CN205182739U - Reation kettle feed distribution ware - Google Patents
Reation kettle feed distribution ware Download PDFInfo
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- CN205182739U CN205182739U CN201521002036.XU CN201521002036U CN205182739U CN 205182739 U CN205182739 U CN 205182739U CN 201521002036 U CN201521002036 U CN 201521002036U CN 205182739 U CN205182739 U CN 205182739U
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- looped pipeline
- pipeline structure
- reactor
- controlled valve
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Abstract
The utility model relates to a chemical industry distributor technical field discloses a reation kettle feed distribution ware, including annular pipe way structure, feeding branch pipe, feeding house steward, automatically controlled valve, annular pipe says that the structure is more than 2 layers or 2 layers, and all is connected with reactor inner wall, annular pipe says that the interior side surface of structure is provided with the atomizing nozzle who is on a parallel with the interior liquid level orientation of reation kettle, every layer of annular pipe says that the structure is all through the total union coupling of feeding branch pipe and feeding, it all is equipped with automatically controlled valve on the feeding branch pipe of structural connection to say with every layer of annular pipe, automatically controlled valve all is located reation kettle is outside, the beneficial effects of the utility model are that: according to actual need and conclusion (of pressure testing), the feeding volume of every layer of distributor of hierarchical control guarantees that the material molecule obtains shifting in the shortest time, improved reaction rate, has reduced reaction period, has improved the product quality.
Description
Technical field
The utility model relates to chemical industry distributor technical field, particularly a kind of reactor feed distributor.
Background technology
In the reactor producing surfactant, draw reactant by two or more liquid phase material complete reaction in reactor.Each liquid phase material should produce large exposed area as far as possible, and mutually fully contact thus reach the object of complete reaction.For reaching this object, need on the one hand to stir fully; On the other hand, feed distributor reasonable, scientific design is also extremely important, the feeder of scientific design can abundant dispersed material, and then reaches the object of complete reaction.In prior art, material enters in reactor the effect not reaching fully dispersion by feed pipe.
Utility model content
The purpose of this utility model is: for the above-mentioned problems in the prior art, provides a kind of reactor feed distributor.
A kind of reactor feed distributor of the utility model, comprises looped pipeline structure, feed-inputing branched pipe, charging house steward, electrically-controlled valve; Described looped pipeline structure is more than 2 layers or 2 layers, and is all connected with reactor inwall; Described looped pipeline structure inner surface is provided with the atomizer being parallel to liquid level direction in reactor; Every layer of looped pipeline structure is all connected with charging house steward by feed-inputing branched pipe; Electrically-controlled valve is equipped with on the feed-inputing branched pipe of every layer of looped pipeline anatomical connectivity; It is outside that described electrically-controlled valve is all positioned at described reactor.
Further, the quantity of the atomizer of every layer of looped pipeline structure is 60, is uniformly distributed in the inner side of looped pipeline structure.
Further, the quantity of looped pipeline structure is 3 layers.
Further, the agitator in reactor haves three layers stirring vane, and every layer of stirring vane is corresponding with equivalent layer looped pipeline structure; Every layer of stirring vane is positioned at equivalent layer looped pipeline structure upper 20cm place.
The beneficial effects of the utility model are: according to actual needs and conclusion (of pressure testing), the inlet amount of hierarchical control every layer distributor, ensure that material molecule is shifted within the shortest time, improve reaction rate, reduce reaction time, improve product quality.
Accompanying drawing explanation
Figure 1 shows that a kind of reactor feed distributor of the utility model structural representation.
In figure: 1-reactor, 2-looped pipeline structure, 3-feed-inputing branched pipe, 4-electrically-controlled valve, 5-charging house steward.
Detailed description of the invention
Hereafter will describe the utility model specific embodiment in detail in conjunction with concrete accompanying drawing.It should be noted that the combination of technical characteristic or the technical characteristic described in following embodiment should not be considered to isolated, they can mutually be combined thus be reached better technique effect.In the accompanying drawing of following embodiment, the identical label that accompanying drawing occurs represents identical feature or parts, can be applicable in different embodiment.
As shown in Figure 1, a kind of reactor feed distributor of the utility model embodiment, comprises looped pipeline structure 2, feed-inputing branched pipe 3, charging house steward 5, electrically-controlled valve 4; Described looped pipeline structure 2 is more than 2 layers or 2 layers, and is all connected with reactor 1 inwall; Described looped pipeline structure 2 inner surface is provided with the atomizer being parallel to liquid level direction in reactor; Every layer of looped pipeline structure 2 is all connected with charging house steward 5 by feed-inputing branched pipe 3; The feed-inputing branched pipe 3 be connected with every layer of looped pipeline structure 2 is equipped with electrically-controlled valve 4; It is outside that described electrically-controlled valve 4 is all positioned at described reactor 1.
Preferably, the quantity of the atomizer of every layer of looped pipeline structure 2 is 60, is uniformly distributed in the inner side of looped pipeline structure 2.
Commonly use, the quantity of looped pipeline structure 2 is 3 layers; Agitator in reactor 1 haves three layers stirring vane, and every layer of stirring vane is corresponding with equivalent layer looped pipeline structure 2; Every layer of stirring vane is positioned at 20cm place, equivalent layer looped pipeline structure 2 top.
In the present embodiment, the quantity of looped pipeline structure 2 is 3 layers, and the nozzle quantity of every layer of looped pipeline structure 2 is 60, totally 180, can ensure that charging is shifted within the shortest time;
During use, material enters feed-inputing branched pipe 3 from charging house steward 5, enters looped pipeline structure 2 through electrically-controlled valve 4, then enters in reactor 1 by the atomizer be arranged in every layer of looped pipeline structure 2; Electrically-controlled valve 4 can control the spray volume of material at every layer of atomizer, and this material spray volume can adjust according to actual needs, also can set according to the conclusion (of pressure testing) for differential responses material.
The beneficial effects of the utility model are: according to actual needs and conclusion (of pressure testing), the inlet amount of hierarchical control every layer distributor, ensure that material molecule is shifted within the shortest time, improve reaction rate, reduce reaction time, improve product quality.
Although given an embodiment of the present utility model, it will be understood by those of skill in the art that when not departing from the utility model spirit herein, can change embodiment herein.Above-described embodiment is exemplary, should using embodiment herein as the restriction of the utility model interest field.
Claims (4)
1. a reactor feed distributor, is characterized in that, comprises looped pipeline structure, feed-inputing branched pipe, charging house steward, electrically-controlled valve; Described looped pipeline structure is more than 2 layers or 2 layers, and is all connected with reactor inwall; Described looped pipeline structure inner surface is provided with the atomizer being parallel to liquid level direction in reactor; Every layer of looped pipeline structure is all connected with charging house steward by feed-inputing branched pipe; Electrically-controlled valve is equipped with on the feed-inputing branched pipe of every layer of looped pipeline anatomical connectivity; It is outside that described electrically-controlled valve is all positioned at described reactor.
2. reactor feed distributor as claimed in claim 1, it is characterized in that, the quantity of the atomizer of every layer of looped pipeline structure is 60, is uniformly distributed in the inner side of looped pipeline structure.
3. reactor feed distributor as claimed in claim 1 or 2, it is characterized in that, the quantity of looped pipeline structure is 3 layers.
4. reactor feed distributor as claimed in claim 3, is characterized in that, the agitator in reactor haves three layers stirring vane, and every layer of stirring vane is corresponding with equivalent layer looped pipeline structure; Every layer of stirring vane is positioned at equivalent layer looped pipeline structure upper 20cm place.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521002036.XU CN205182739U (en) | 2015-12-04 | 2015-12-04 | Reation kettle feed distribution ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521002036.XU CN205182739U (en) | 2015-12-04 | 2015-12-04 | Reation kettle feed distribution ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205182739U true CN205182739U (en) | 2016-04-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521002036.XU Expired - Fee Related CN205182739U (en) | 2015-12-04 | 2015-12-04 | Reation kettle feed distribution ware |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205182739U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108295799A (en) * | 2018-03-28 | 2018-07-20 | 苏州市锦翔压力容器制造有限公司 | A kind of efficient polyether reactant device |
| CN109550475A (en) * | 2018-10-19 | 2019-04-02 | 兖矿鲁南化工有限公司 | A kind of acetic acid reaction kettle fluid mixing system |
| CN109772236A (en) * | 2017-11-14 | 2019-05-21 | 中国石油化工股份有限公司 | A kind of fluid distributor, reaction unit and its application |
| CN109894068A (en) * | 2019-03-14 | 2019-06-18 | 浙江辽想新材料科技有限公司 | A kind of reaction kettle of evenly dispersed material |
| CN109894070A (en) * | 2019-03-14 | 2019-06-18 | 浙江辽想新材料科技有限公司 | A kind of dynamic respons kettle |
-
2015
- 2015-12-04 CN CN201521002036.XU patent/CN205182739U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109772236A (en) * | 2017-11-14 | 2019-05-21 | 中国石油化工股份有限公司 | A kind of fluid distributor, reaction unit and its application |
| WO2019096065A1 (en) * | 2017-11-14 | 2019-05-23 | 中国石油化工股份有限公司 | Fluid distributor, reaction device, and application thereof |
| CN109772236B (en) * | 2017-11-14 | 2022-08-12 | 中国石油化工股份有限公司 | Fluid distributor, reaction device and application thereof |
| US11571673B2 (en) | 2017-11-14 | 2023-02-07 | China Petroleum & Chemical Corporation | Fluid distributor, reaction device and application thereof |
| CN108295799A (en) * | 2018-03-28 | 2018-07-20 | 苏州市锦翔压力容器制造有限公司 | A kind of efficient polyether reactant device |
| CN108295799B (en) * | 2018-03-28 | 2024-06-21 | 苏州市锦翔压力容器制造有限公司 | High-efficiency polyether reactor |
| CN109550475A (en) * | 2018-10-19 | 2019-04-02 | 兖矿鲁南化工有限公司 | A kind of acetic acid reaction kettle fluid mixing system |
| CN109550475B (en) * | 2018-10-19 | 2020-04-28 | 兖矿鲁南化工有限公司 | Fluid mixing system of acetic acid reaction kettle |
| CN109894068A (en) * | 2019-03-14 | 2019-06-18 | 浙江辽想新材料科技有限公司 | A kind of reaction kettle of evenly dispersed material |
| CN109894070A (en) * | 2019-03-14 | 2019-06-18 | 浙江辽想新材料科技有限公司 | A kind of dynamic respons kettle |
| CN109894068B (en) * | 2019-03-14 | 2021-06-22 | 浙江辽想新材料科技有限公司 | Reation kettle of homodisperse material |
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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: 20160427 |