CN204891884U - Spraying tower reactor - Google Patents
Spraying tower reactor Download PDFInfo
- Publication number
- CN204891884U CN204891884U CN201520489803.8U CN201520489803U CN204891884U CN 204891884 U CN204891884 U CN 204891884U CN 201520489803 U CN201520489803 U CN 201520489803U CN 204891884 U CN204891884 U CN 204891884U
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- China
- Prior art keywords
- connector body
- gas
- ware
- distributor
- gaseous
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- 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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Abstract
The utility model discloses a spraying tower reactor, be by the ware body, gas outlet, demister, liquid inlet, again cloth ware, downspout, gaseous one -level distributor, gaseous second grade distributor, gas access, liquid inlet and fluid -discharge tube constitute, flowing back tube connector body right side below, liquid outlet connector body left side below, the liquid outlet is connected with the fluid -discharge tube internal of ware, gas access connector body right side, inside the gaseous one -level distributor connector body, the gas access is located the internal portion of ware and is connected with gaseous one -level distributor, the gaseous inside top that is located gaseous one -level distributor of second grade distributor connector body, the downspout is located the internal portion of ware left side, again above the cloth ware connector body inside, liquid inlet connector body right side top, the inside top of demister connector body, the gas outlet is located the external portion top of ware, the ware body for stainless steel. The utility model discloses simple structure, convenient to use, the technique is reasonable.
Description
Technical field
The utility model belongs to a kind of chemical industry equipment, is specifically related to a kind of spraying tower reactor.
Background technology
Constantly sulfur dioxide reaction generation sulfur trioxide is studied and put into practice in domestic and international gas washing in SA production and PRODUCTION TRAITS process, the layout of positive discussion heat power equipment and reactor and structural adjustment, from increasing air Quench between reactor catalyst bed to regulate temperature to arranging central tube at reactor for supporting and arranging heat power equipment in central tube thus reduce heat power equipment or reduce heat power equipment disposed outside thus avoid the external defect of bringing of heat power equipment as far as possible, for device stable operation creates conditions; But adopt air Quench structure just cannot utilize reaction heat, the built-in heat power equipment of central tube effectively solves external defect, but simultaneously because arranging of central tube produces comparatively adverse effect to distribution of gas, thus affect catalyst reaction efficiency; They use all certain defect and limitation.
Utility model content
The purpose of this utility model is to provide a kind of spraying tower reactor, to solve the deficiency existed in above-mentioned technology.
In order to achieve the above object, the technical scheme that the utility model adopts is:
A kind of spraying tower reactor, by body, gas vent, demister, liquid inlet, cloth device again, downspout, gas primary distributor, gas secondary distributor, gas access, liquid outlet and discharging tube composition, described discharging tube connector body lower right-hand side, below on the left of liquid outlet connector body, liquid outlet is connected with discharging tube in body inside, on the right side of the connector body of gas access, gas primary distributor connector body is inner, gas access is positioned at body inside and is connected with gas primary distributor, gas secondary distributor connector body inside is positioned at the top of gas primary distributor, downspout is positioned at body inside left, cloth device connector body inner upper again, top on the right side of the connector body of liquid inlet, demister connector body inner upper, gas vent is positioned at body outer tip end.
Described body is stainless steel.
The utility model structure is simple, and easy to use, technology is reasonable.Provide the stable condition of device to gas washing in SA production, reduce production cost and saved investment in land because heat power equipment is built-in simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
As shown in Figure 1, a kind of spraying tower reactor, by body 1, gas vent 2, demister 3, liquid inlet 4, cloth device 5 again, downspout 6, gas primary distributor 7, gas secondary distributor 8, gas access 9, liquid outlet 10 and discharging tube 11 form, described discharging tube 11 connector body 1 lower right-hand side, below on the left of liquid outlet 10 connector body 1, liquid outlet 10 is connected with discharging tube 11 in body 1 inside, on the right side of gas access 9 connector body 1, gas primary distributor 7 connector body 1 is inner, gas access 9 is positioned at body 1 inside and is connected with gas primary distributor 7, gas secondary distributor 8 connector body 1 inside is positioned at the top of gas primary distributor 7, downspout 6 is positioned at body 1 inside left, cloth device 5 connector body 1 inner upper again, top on the right side of liquid inlet 4 connector body 1, demister 3 connector body 1 inner upper, gas vent 2 is positioned at body 1 outer tip end, described body 1 is stainless steel.
Claims (2)
1. a spraying tower reactor, by body, gas vent, demister, liquid inlet, cloth device again, downspout, gas primary distributor, gas secondary distributor, gas access, liquid outlet and discharging tube composition, it is characterized in that: described discharging tube connector body lower right-hand side, below on the left of liquid outlet connector body, liquid outlet is connected with discharging tube in body inside, on the right side of the connector body of gas access, gas primary distributor connector body is inner, gas access is positioned at body inside and is connected with gas primary distributor, gas secondary distributor connector body inside is positioned at the top of gas primary distributor, downspout is positioned at body inside left, cloth device connector body inner upper again, top on the right side of the connector body of liquid inlet, demister connector body inner upper, gas vent is positioned at body outer tip end.
2. one spraying tower reactor according to claim 1, is characterized in that: described body is stainless steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520489803.8U CN204891884U (en) | 2015-07-09 | 2015-07-09 | Spraying tower reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520489803.8U CN204891884U (en) | 2015-07-09 | 2015-07-09 | Spraying tower reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204891884U true CN204891884U (en) | 2015-12-23 |
Family
ID=54914099
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520489803.8U Expired - Fee Related CN204891884U (en) | 2015-07-09 | 2015-07-09 | Spraying tower reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204891884U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107162882A (en) * | 2017-07-04 | 2017-09-15 | 中国科学院过程工程研究所 | Spray column disc type reactor, system and technique with its production propylene glycol monomethyl ether |
| CN109395499A (en) * | 2018-10-26 | 2019-03-01 | 周贵英 | A kind of dry desulfurization reaction tower |
-
2015
- 2015-07-09 CN CN201520489803.8U patent/CN204891884U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107162882A (en) * | 2017-07-04 | 2017-09-15 | 中国科学院过程工程研究所 | Spray column disc type reactor, system and technique with its production propylene glycol monomethyl ether |
| CN107162882B (en) * | 2017-07-04 | 2020-10-02 | 中国科学院过程工程研究所 | Spray tower tray type reactor, system and process for producing propylene glycol monomethyl ether by using same |
| CN109395499A (en) * | 2018-10-26 | 2019-03-01 | 周贵英 | A kind of dry desulfurization reaction tower |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151223 Termination date: 20160709 |