CN212142536U - Process unit for preparing isobutene - Google Patents
Process unit for preparing isobutene Download PDFInfo
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- CN212142536U CN212142536U CN202020684874.4U CN202020684874U CN212142536U CN 212142536 U CN212142536 U CN 212142536U CN 202020684874 U CN202020684874 U CN 202020684874U CN 212142536 U CN212142536 U CN 212142536U
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- catalytic distillation
- distillation tower
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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 process unit for preparing isobutene, which comprises a catalytic distillation tower, a cooler, a buffer tank and a production pump which are connected in sequence; tertiary butanol enters the catalytic distillation tower from a feed inlet at the upper part of the tower and is dehydrated under the catalytic action of a resin catalyst in the tower to generate isobutene; the removed water is extracted from a discharge port II at the bottom of the catalytic distillation tower, the extracted water is divided into two parts, one part of the water flows through a reboiler and then returns to the catalytic distillation tower from a reboiling material inlet to realize the reboiling function, and the other part of the water is directly extracted into a water treatment device; the generated isobutene is extracted from a discharge port I at the top of the catalytic distillation tower, is cooled by a cooler and then enters a buffer tank, and is extracted by an extraction pump and then divided into two parts, wherein one part flows back to the catalytic distillation tower from a reflux port, and the other part is extracted as a product. The utility model has simple process, easy operation, high conversion per pass, and reduced energy consumption and equipment investment.
Description
Technical Field
The utility model relates to a process units of preparation isobutene.
Background
Isobutene, also known as 2-methylpropene, is an important chemical raw material which is mainly used for preparing butyl rubber, polyisobutylene, methacrylonitrile, an antioxidant, tert-butyl phenol, tert-butyl ether and the like. The method for producing isobutene comprises C4 fraction separation, tert-butyl alcohol dehydration, MTBE cracking and the like. Wherein, the C4 fraction is separated, and isobutene with higher purity is difficult to obtain. Although high-purity isobutene can be obtained by MTBE cracking, the separation and purification process is complex and the energy consumption is relatively high. The tertiary butanol dehydration method can not only obtain high-purity isobutene, but also has the advantages of simple process, less side reaction, easy separation and refining and low operation cost. Therefore, the tertiary butanol dehydration method has good prospect, but the prior tertiary butanol dehydration method has lower conversion per pass.
Disclosure of Invention
The utility model aims to solve the technical problem that to the not enough of existence among the prior art, and provide a process units of preparation isobutene, the utility model discloses simple process, easy to operate, its one-way conversion rate are high, have reduced energy consumption and equipment investment.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a process units of preparation isobutene, is including the catalytic distillation tower, cooler, buffer tank, the extraction pump that connect gradually, its characterized in that:
the catalytic distillation tower is provided with a discharge port I at the tower top and a discharge port II at the tower bottom; a feed inlet is arranged at the upper part of one side of the tower wall, a reflux port is arranged at the upper part of the other side of the tower wall, and the position of the reflux port is higher than that of the feed inlet; wherein: the feed inlet is connected with a device for providing tert-butyl alcohol; the discharge port II is connected with a water treatment device; the discharge port I is sequentially connected with the cooler, the buffer tank and the extraction pump; the pump outlet of the extraction pump is divided into two paths, one path is connected with the reflux port, and the other path is connected with the isobutene recovery device.
In the above-mentioned technical means, the catalytic distillation column has a reboiler disposed at the lower part of the column wall.
In the technical scheme, the lower part of the tower wall of the catalytic distillation tower is provided with a reboiling material inlet, and the discharge port II is connected with a water treatment device and is also divided into a path which is connected with the reboiling material inlet through a reboiler so as to realize the reboiling effect.
In the above technical solution, the catalytic distillation column is filled with a resin catalyst, preferably a sulfonic acid resin catalyst, and more preferably a macroporous sulfonic acid resin catalyst.
The utility model also provides a process method for preparing isobutene, including following step: tertiary butanol enters the catalytic distillation tower from a feed inlet at the upper part of the tower and is dehydrated under the catalytic action of a resin catalyst in the tower to generate isobutene; the removed water is extracted from a discharge port II at the bottom of the catalytic distillation tower, the extracted water is divided into two parts, one part of the water flows through a reboiler and then returns to the catalytic distillation tower from a reboiling material inlet to realize the reboiling function, and the other part of the water is directly extracted into a water treatment device; the generated isobutene is extracted from a discharge port I at the top of the catalytic distillation tower, is cooled by a cooler and then enters a buffer tank, and is extracted by an extraction pump and then divided into two parts, wherein one part flows back to the catalytic distillation tower from a reflux port, and the other part is extracted as a product.
In the technical scheme, the feeding temperature of the tert-butyl alcohol is 20-30 ℃, and preferably 25 ℃.
In the technical scheme, the feeding pressure of the tert-butyl alcohol is 5-15 bar, preferably 10 bar.
In the technical scheme, the feeding mass space velocity of the tert-butyl alcohol is 0.5-6h-1。
In the above technical solution, the resin catalyst is a high temperature resistant resin catalyst, preferably a D006 type or D008 type resin catalyst.
In the technical scheme, the temperature of the top of the catalytic distillation tower is 50-55 ℃, and is preferably 53.77 ℃.
In the technical scheme, the pressure at the top of the catalytic distillation tower is 4-6 bar, preferably 5 bar.
In the technical scheme, the bottom temperature of the catalytic distillation tower is 150-160 ℃, and 159 ℃ is preferred.
In the technical scheme, the pressure at the bottom of the catalytic distillation tower is 5-8 bar, preferably 6 bar.
In the technical scheme, the isobutene is extracted from a discharge port I at the top of the catalytic distillation tower, cooled by a cooler and then enters a buffer tank, and the cooling temperature is 40-45 ℃, and is preferably 42.7 ℃.
In the technical scheme, a part of isobutene extracted by an extraction pump flows back to the catalytic distillation tower through a reflux port, and the reflux ratio is 1-10: 1.
the utility model discloses technical scheme's advantage lies in: the utility model discloses a catalytic distillation technique is to tert butyl alcohol dehydration system isobutene, and the catalyst adopts resin catalyst, and this method simple process, easy to operate, its per pass conversion is high, has reduced energy consumption and equipment investment.
Drawings
FIG. 1: is a schematic diagram of the whole structure of the process device for preparing the isobutene;
wherein, 1, catalytic distillation tower, 2, reboiler, 3, cooler, 4, buffer tank, 5, extraction pump, 6, feed inlet, 7, discharge gate I, 8, backward flow mouth, 9, discharge gate II, 10, reboiling material import.
Detailed Description
The following detailed description of the embodiments of the present invention, but the present invention is not limited to the following description:
the utility model discloses at first provide a process units of preparation isobutene, including catalytic distillation tower 1, cooler 3, buffer tank 4, the extraction pump 5 that connects gradually, as shown in figure 1:
the catalytic distillation tower 1 is provided with a discharge port I7 at the tower top and a discharge port II9 at the tower bottom; a feed inlet 6 is arranged at the upper part of one side of the tower wall, a reflux opening 8 is arranged at the upper part of the other side of the tower wall, and the position of the reflux opening is higher than that of the feed inlet; wherein: the feed inlet is connected with a device for providing tert-butyl alcohol; the discharge port II is connected with a water treatment device; the discharge port I is sequentially connected with the cooler, the buffer tank and the extraction pump; the outlet of the extraction pump is divided into two paths, one path is connected with the reflux port, and the other path is connected with the isobutene recovery device;
the lower part of the tower wall of the catalytic distillation tower is provided with a reboiler 2;
the lower part of the tower wall of the catalytic distillation tower is provided with a reboiling material inlet 10, and the discharge port II is connected with a water treatment device and is also divided into a path to be connected with the reboiling material inlet through a reboiler 2 so as to realize the reboiling effect;
the catalytic distillation tower is filled with a resin catalyst, wherein the resin catalyst is a high-temperature resistant resin catalyst, and preferably a D006 type or D008 type resin catalyst.
The utility model also provides a process method for preparing isobutene, including following step: tertiary butanol enters the catalytic distillation tower from a feed inlet at the upper part of the tower and is dehydrated under the catalytic action of a resin catalyst in the tower to generate isobutene; the removed water is extracted from a discharge port II at the bottom of the catalytic distillation tower, the extracted water is divided into two parts, one part of the water flows through a reboiler and then returns to the catalytic distillation tower from a reboiling material inlet to realize the reboiling function, and the other part of the water is directly extracted into a water treatment device; the generated isobutene is extracted from a discharge port I at the top of the catalytic distillation tower, is cooled by a cooler and then enters a buffer tank, and is extracted by an extraction pump and then divided into two parts, wherein one part flows back to the catalytic distillation tower from a reflux port, and the other part is extracted as a product.
The invention will be elucidated with reference to specific embodiments.
Example 1:
a process for preparing isobutene includes feeding tert-butanol from tank region from the upper part of catalytic distillation tower at 25 deg.C and 10bar at air speed of 3 hr-1(ii) a Dehydrating under the catalytic action of a D008 type resin catalyst to generate isobutene, wherein the tower top temperature of the catalytic distillation tower is 53.77 ℃, the tower top pressure is 5bar, the tower bottom temperature is 159 ℃, and the tower bottom pressure is 6 bar; the removed water is extracted from a discharge port II at the bottom of the catalytic distillation tower, the extracted water is divided into two parts, one part is returned to the catalytic distillation tower through a reboiling material inlet to realize reboiling, and the other part is directly extracted; the generated isobutene is extracted from a discharge port I at the top of the catalytic distillation tower, cooled to 42.7 ℃ by a cooler and then enters a buffer tank, and then extracted by an extraction pump and then divided into two parts, wherein one part is refluxed into the catalytic distillation tower from a reflux port (the reflux ratio is 5: 1), and the other part is extracted as a product.
In this example, the conversion of tert-butanol was 99.8%, and the overall yield was 98.6%.
The above examples are merely illustrative of the technical concept and technical features of the present invention, and thus the scope of the present invention is not limited thereto. All equivalent changes and modifications made according to the spirit of the present invention should be covered within the protection scope of the present invention.
Claims (6)
1. The technical device for preparing the isobutene comprises a catalytic distillation tower (1), a cooler (3), a buffer tank (4) and a production pump (5) which are sequentially connected, and is characterized in that:
the catalytic distillation tower (1) is provided with a discharge port I (7) at the top and a discharge port II (9) at the bottom; a feed inlet (6) is arranged at the upper part of one side of the tower wall, a reflux opening (8) is arranged at the upper part of the other side of the tower wall, and the position of the reflux opening is higher than that of the feed inlet; wherein: the feed inlet is connected with a device for providing tert-butyl alcohol; the discharge port II is connected with a water treatment device; the discharge port I is sequentially connected with the cooler, the buffer tank and the extraction pump; the pump outlet of the extraction pump is divided into two paths, one path is connected with the reflux port, and the other path is connected with the isobutene recovery device.
2. The process arrangement of claim 1, wherein: the catalytic distillation tower is provided with a reboiler (2) at the lower part of the tower wall.
3. The process arrangement according to claim 1 or 2, characterized in that: the catalytic distillation tower is characterized in that a reboiling material inlet (10) is formed in the lower portion of the tower wall, the discharge port II is connected with a water treatment device, and a reboiler (2) is connected with the reboiling material inlet to achieve the reboiling effect.
4. The process arrangement of claim 1, wherein: the catalytic distillation tower is filled with a resin catalyst.
5. The process arrangement of claim 4, wherein: the resin catalyst is a high-temperature resistant resin catalyst.
6. The process arrangement of claim 5, wherein: the high-temperature resistant resin catalyst is a D006 type or D008 type resin catalyst.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202020684874.4U CN212142536U (en) | 2020-04-29 | 2020-04-29 | Process unit for preparing isobutene |
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| CN202020684874.4U CN212142536U (en) | 2020-04-29 | 2020-04-29 | Process unit for preparing isobutene |
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| CN212142536U true CN212142536U (en) | 2020-12-15 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111530379A (en) * | 2020-04-29 | 2020-08-14 | 凯瑞环保科技股份有限公司 | Process method and process device for preparing isobutene |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111530379A (en) * | 2020-04-29 | 2020-08-14 | 凯瑞环保科技股份有限公司 | Process method and process device for preparing isobutene |
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