CN105152235B - A kind of multistage inner circulation reactor of chemical industry - Google Patents
A kind of multistage inner circulation reactor of chemical industry Download PDFInfo
- Publication number
- CN105152235B CN105152235B CN201510509892.2A CN201510509892A CN105152235B CN 105152235 B CN105152235 B CN 105152235B CN 201510509892 A CN201510509892 A CN 201510509892A CN 105152235 B CN105152235 B CN 105152235B
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- CN
- China
- Prior art keywords
- reactor
- multistage
- reative cell
- chemical industry
- inner circulation
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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.)
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Abstract
The present invention relates to a kind of multistage inner circulation reactor of chemical industry, belong to technical field of chemical.A kind of multistage inner circulation reactor of chemical industry, including multistage reactor, reative cell, collector, multistage reactor is connected with recover, recover is made up of housing and end socket, and housing lower end is provided with supporting leg, and multistage reactor is provided with backflow control system, reative cell is arranged at the top of multistage reactor, reative cell is joined directly together with multistage reactor, and reative cell bottom is provided with outlet close to both sides Board position, and collector is connected by connecting tube with reative cell.The beneficial effects of the invention are as follows：Pipeline is simple, and the resistance of ducting is small, and system vacuum is high, and line loss is small, easy to operate, reaction rate is high, and the dischargeable capacity of reactor is big, can more thoroughly be reacted, so as to reduce sewage discharge.
Description
Technical field
The present invention relates to a kind of multistage inner circulation reactor of chemical industry, belong to technical field of chemical.
Background technology
Inner circulation reactor is just acknowledged as with rate of load condensate is high, ratio of height to diameter is big, floor space from starting to be utilized
The characteristics such as small, capital expenditure province, stable performance, thus by the generally accreditation of chemical industry, but existing interior circular response
For device also there is the problems such as reaction rate is low, dischargeable capacity of reactor is small, caused waste water is more, environment is polluted, to production
Many problems are all brought with life.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of chemical industry with multistage inner circulation reactor, make its is simple in construction,
Easy to operate, raising reaction rate, reduces discharge of wastewater.
The present invention is achieved by the following technical solutions：
A kind of multistage inner circulation reactor of chemical industry, it is characterized in that, including multistage reactor 8, reative cell 5, receipts
Storage 3, multistage reactor 8 are connected with recover, and recover is made up of housing 9 and end socket 10, and the lower end of housing 9 is provided with supporting leg
11, for multistage reactor 8 provided with backflow control system 7, reative cell 5 is arranged on the top of multistage reactor 8, reative cell 5 and multistage
Reactor 8 is joined directly together, and the bottom of reative cell 5 is provided with outlet 13 close to both sides Board position, and collector 3 is by connecting tube 4 and instead
Room 5 is answered to connect；
The housing 9 is provided with hand hole 12；
First baffle 2 is provided with the collector 3；
Second baffle 6 is provided with the reative cell 5；
Charging aperture 1, medium inlet 16 and exhaust outlet 15 are respectively arranged with the collector 3；
The right side of reative cell 5 is provided with water inlet 14.
The beneficial effects of the invention are as follows：Pipeline is simple, and the resistance of ducting is small, and system vacuum is high, and line loss is small, operation letter
Just, reaction rate is high, and the dischargeable capacity of reactor is big, can more thoroughly be reacted, so as to reduce sewage discharge.
Brief description of the drawings
Fig. 1 is the multistage inner circulation reactor structural representation of chemical industry of the invention.
In figure：1st, charging aperture；2nd, first baffle；3rd, collector；4th, connecting tube；5th, reative cell；6th, second baffle；7th, flow back
Control system；8th, multistage reactor；9th, housing；10th, end socket；11st, supporting leg；12nd, hand hole；13rd, outlet；14th, water inlet；15、
Exhaust outlet；16th, medium inlet.
Embodiment
A kind of multistage inner circulation reactor of chemical industry of the present embodiment, including multistage reactor 8, reative cell 5, collector 3,
Multistage reactor 8 is connected with recover, and recover is made up of housing 9 and end socket 10, and the lower end of housing 9 is provided with supporting leg 11, multistage
Reactor 8 is provided with backflow control system 7, and reative cell 5 is arranged on the top of multistage reactor 8, reative cell 5 and multistage reactor 8
It is joined directly together, the bottom of reative cell 5 is provided with outlet 13 close to both sides Board position, and collector 3 is connected by connecting tube 4 and reative cell 5
It is logical；
The housing 9 is provided with hand hole 12；
First baffle 2 is provided with the collector 3；
Second baffle 6 is provided with the reative cell 5；
Charging aperture 1, medium inlet 16 and exhaust outlet 15 are respectively arranged with the collector 3；
The right side of reative cell 5 is provided with water inlet 14.
Operation principle：Chemical substance reduces the discharge of sewage, being realized in inside reactor need not after reaction of high order
The interior circulation of additionaling power, so as to strengthen mass transfer effect, improves reaction rate, and having for reactor is just the increase at one
Imitate volume.
The beneficial effects of the invention are as follows：Pipeline is simple, and the resistance of ducting is small, and system vacuum is high, and line loss is small, operation letter
Just, reaction rate is high, and the dischargeable capacity of reactor is big, can more thoroughly be reacted, so as to reduce sewage discharge.
The foregoing is only presently preferred embodiments of the present invention, be not intended to limit the invention, it is all the present invention spirit and
Any modification, equivalent substitution and improvements made within principle etc., should be included in the scope of the protection.
Claims (6)
1. the multistage inner circulation reactor of a kind of chemical industry, it is characterised in that including multistage reactor（8）, reative cell（5）, collector
（3）, multistage reactor（8）It is connected with recover, recover is by housing（9）And end socket（10）Composition, housing（9）Lower end is provided with
Supporting leg（11）, multistage reactor（8）It is provided with backflow control system（7）, reative cell（5）Installed in multistage reactor（8）Top,
Reative cell（5）With multistage reactor（8）It is joined directly together, reative cell（5）Bottom is provided with outlet close to both sides Board position（13）, receive
Storage（3）Pass through connecting tube（4）With reative cell（5）Connection.
A kind of 2. multistage inner circulation reactor of chemical industry according to claim 1, it is characterised in that the housing（9）It is provided with
Hand hole（12）.
A kind of 3. multistage inner circulation reactor of chemical industry according to claim 1, it is characterised in that the collector（3）Inside set
There is first baffle（2）.
A kind of 4. multistage inner circulation reactor of chemical industry according to claim 1, it is characterised in that the reative cell（5）Inside set
There is second baffle（6）.
A kind of 5. multistage inner circulation reactor of chemical industry according to claim 1, it is characterised in that the collector（3）Upper point
Charging aperture is not provided with it（1）, medium inlet（16）And exhaust outlet（15）.
A kind of 6. multistage inner circulation reactor of chemical industry according to claim 1, it is characterised in that the reative cell（5）Right side
Provided with water inlet（14）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510509892.2A CN105152235B (en) | 2015-08-19 | 2015-08-19 | A kind of multistage inner circulation reactor of chemical industry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510509892.2A CN105152235B (en) | 2015-08-19 | 2015-08-19 | A kind of multistage inner circulation reactor of chemical industry |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105152235A CN105152235A (en) | 2015-12-16 |
| CN105152235B true CN105152235B (en) | 2017-12-08 |
Family
ID=54793363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510509892.2A Expired - Fee Related CN105152235B (en) | 2015-08-19 | 2015-08-19 | A kind of multistage inner circulation reactor of chemical industry |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105152235B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4329234A (en) * | 1980-04-15 | 1982-05-11 | Exxon Research & Engineering Co. | Multi-stage gas liquid reactor |
| US8017095B2 (en) * | 2009-05-29 | 2011-09-13 | Chevron U.S.A. Inc. | Mixing device for a down-flow reactor |
| CN202508922U (en) * | 2012-03-29 | 2012-10-31 | 中国石油化工股份有限公司 | Adjustable anaerobic internal circulation reactor |
| CN202594856U (en) * | 2011-11-28 | 2012-12-12 | 广西大学 | Internal recycling reactor capable of being adjusted and reinforced |
| CN103480316A (en) * | 2013-10-18 | 2014-01-01 | 洛阳昶威机械制造安装有限公司 | Novel high-efficiency internal circulation reactor |
-
2015
- 2015-08-19 CN CN201510509892.2A patent/CN105152235B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4329234A (en) * | 1980-04-15 | 1982-05-11 | Exxon Research & Engineering Co. | Multi-stage gas liquid reactor |
| US8017095B2 (en) * | 2009-05-29 | 2011-09-13 | Chevron U.S.A. Inc. | Mixing device for a down-flow reactor |
| CN202594856U (en) * | 2011-11-28 | 2012-12-12 | 广西大学 | Internal recycling reactor capable of being adjusted and reinforced |
| CN202508922U (en) * | 2012-03-29 | 2012-10-31 | 中国石油化工股份有限公司 | Adjustable anaerobic internal circulation reactor |
| CN103480316A (en) * | 2013-10-18 | 2014-01-01 | 洛阳昶威机械制造安装有限公司 | Novel high-efficiency internal circulation reactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105152235A (en) | 2015-12-16 |
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Effective date of registration: 20170721 Address after: 510640 Guangdong City, Tianhe District Province, No. five, road, public education building, unit 371-1, unit 2401 Applicant after: Guangdong Gaohang Intellectual Property Operation Co., Ltd. Address before: Laixi City, Shandong province 266699 Longkou Road Qingdao City, No. 28 Applicant before: Sun Limin |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20171013 Address after: 325802 development road 1-85, Longgang new town, Cangnan County, Zhejiang, Wenzhou Applicant after: WENZHOU LIANYI HARNESS ADHESIVE TAPE CO., LTD. Address before: 510640 Guangdong City, Tianhe District Province, No. five, road, public education building, unit 371-1, unit 2401 Applicant before: Guangdong Gaohang Intellectual Property Operation Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171208 Termination date: 20180819 |
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| CF01 | Termination of patent right due to non-payment of annual fee |