CN2604434Y - Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid - Google Patents
Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid Download PDFInfo
- Publication number
- CN2604434Y CN2604434Y CN 03233076 CN03233076U CN2604434Y CN 2604434 Y CN2604434 Y CN 2604434Y CN 03233076 CN03233076 CN 03233076 CN 03233076 U CN03233076 U CN 03233076U CN 2604434 Y CN2604434 Y CN 2604434Y
- Authority
- CN
- China
- Prior art keywords
- tower
- acetic acid
- convertor
- liquid phase
- bubble tower
- Prior art date
- 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 - Lifetime
Links
Images
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses a bubble column converter used at a process for the production of acetic acid by a liquid phase of methanol oxo synthesis under a lower pressure. The utility model mainly consists of a column body and a gas distributor located at the lower section of the column body with a diameter height rate of 5 to 6. The gas distributor is a dual-ring porous gas distributor with a rate of the mean diameter of an external annular pipe to the column diameter at a level from one half to one third. About 80 to 90 per cent holes spray upwards with two neighboring holes forming an included angle from 45 degrees to 60 degrees but a range from 45 degrees to 50 degrees preferred; the rest 20 to 10 per cent holes spray vertically downwards. The utility model is characterized by a well effect of mass transfer, a small outline of reactor and high conversion efficiency.
Description
The utility model belongs to chemical industry equipment, makes the field in particular for the conversion unit of acetic acid synthesis process by low-pressure methanol carbonylation.
Chinese invention patent (ZL92108244.4) provides a kind of low-pressure methanol liquid phase carbonyl acetic acid synthesized method, and being characterized in increases a convertor after the reactor in conventional process flow.After reaction solution enters convertor, proceed carbonylation reaction, the methyl alcohol degree of depth is transformed with the carbon monoxide that adds.But the convertor equipment that does not have at present the use that processing condition with it match.
The purpose of this utility model is, designs the special-purpose bubble tower convertor that a kind of and above technology matches and uses, and makes it to have higher transformation efficiency and good mass transfer effect.
The purpose of this utility model is to realize by following means.
The acetic acid synthesized technology of low-pressure methanol liquid phase carbonyl bubble tower convertor mainly by tower body with place the gas distributor etc. of tower body bottom to form, is characterized in that the blade diameter length ratio of bubble tower convertor is 5～6; The gas distributor of bubble tower convertor is a dicyclic porous gas sparger, and the footpath is 1/2～1/3 with the ratio of tower diameter in its outer endless tube; 80%～90% aperture upwards sprays, and adjacent two holes are at 45 mutually～60 ° of angles, be preferably 45 °～50 ° angles, 20%～10% aperture sprays downward vertically; Aperture is uniform distribution on two rings.
After adopting design as above, effectively mass transfer area improves, and can satisfy the requirement that the degree of depth transforms in the carbonyl synthesis acetic acid technology.
Description of drawings is as follows:
Fig. 1 is the longitudinal sectional view of the utility model embodiment.
Fig. 2 is the part figure of dicyclic porous gas sparger.
Fig. 3 is a dicyclic porous gas sparger position of opening graph of a relation.
Fig. 4 is the longitudinal sectional view of the utility model band self-absorbing type stirrer embodiment.
Below in conjunction with accompanying drawing structure of the present utility model is described in further detail.
Can see in conjunction with Fig. 1, Fig. 2 and Fig. 3, form tower body by inlet pipe 1, escape pipe 2, liquid-blocking device 3, overflow weir 4, drain pipe 5, liquid-leaking nozzle 6, tower tube 7, liquid-inlet pipe 8 etc.The blade diameter length ratio of bubble tower convertor is 5.5; The gas distributor 9 of bubble tower convertor is a dicyclic porous gas sparger, and the footpath is 0.4 (1/2～1/3) with the ratio of tower diameter in its outer endless tube; 90% aperture upwards sprays, and the angle of cut α of the axial connecting line in adjacent two holes is 45 °～60 ° angles, is preferably 45 °～50 ° angles, and 10% aperture sprays downward vertically; Aperture is uniform distribution on two rings.The aperture total sectional area be tower section long-pending 0.35%～0.38%.
Convertor of the present utility model can adopt two kinds of structures: a kind of is the structure of above embodiment, constitutes the full back-mixing in bottom, the streamlined bubble tower in middle and upper part, is applicable to the situation that carbon monoxide pressure of tension is higher; When carbon monoxide pressure of tension in the reactor tail gas is low, adopt the structure of Fig. 4 embodiment, constitute the bubble tower of the full back-mixing in bottom, middle part laminar flow, the self-priming stirring of top band, reaction end gas can be sucked in the liquid phase once again like this, to guarantee the transmission of convertor top carbon monoxide.In Fig. 4, in the structure of a last embodiment, set up a self-absorbing type stirrer 10, mixing device paddle diameter is 1/3～1/2 of tower diameter.
Claims (4)
1, the acetic acid synthesized technology of low-pressure methanol liquid phase carbonyl bubble tower convertor mainly by tower body with place the gas distributor etc. of tower body bottom to form, is characterized in that the blade diameter length ratio of bubble tower convertor is 5～6; The gas distributor of bubble tower convertor is a dicyclic porous gas sparger, and the footpath is 1/2～1/3 with the ratio of tower diameter in its outer endless tube; 80%～90% aperture upwards sprays, and adjacent two holes are at 45 mutually～60 ° of angles; 20%～10% aperture sprays downward vertically; Aperture is uniform distribution on two rings.
2, according to the acetic acid synthesized technology of the described low-pressure methanol liquid phase carbonyl of claim 1 bubble tower convertor, it is characterized in that, described adjacent two holes are at 45 mutually～50 ° of angles.
3, according to the acetic acid synthesized technology of the described low-pressure methanol liquid phase carbonyl of claim 1 bubble tower convertor, it is characterized in that, described aperture total sectional area be tower section long-pending 0.35%～0.38%.
4, according to the acetic acid synthesized technology of the described low-pressure methanol liquid phase carbonyl of claim 1 bubble tower convertor, it is characterized in that tower body top is equipped with self-absorbing type stirrer, agitator paddle diameter is 1/3～1/2 of a tower diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03233076 CN2604434Y (en) | 2003-01-30 | 2003-01-30 | Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03233076 CN2604434Y (en) | 2003-01-30 | 2003-01-30 | Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2604434Y true CN2604434Y (en) | 2004-02-25 |
Family
ID=34165569
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03233076 Expired - Lifetime CN2604434Y (en) | 2003-01-30 | 2003-01-30 | Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2604434Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101885678A (en) * | 2010-07-05 | 2010-11-17 | 兖矿国泰化工有限公司 | Reaction equipment for synthesizing ethylic acid by low-pressure methanol carbonylation of methanol |
| CN101811930B (en) * | 2009-02-19 | 2013-04-03 | 中国石油化工股份有限公司 | Selective hydrogenation method for phenylacetylene in phenylacetylene-containing styrene material flow |
| CN104028177A (en) * | 2013-03-06 | 2014-09-10 | 中石化上海工程有限公司 | Method for reinforcing mixing effect of hydraulic reaction apparatus |
| CN104815593A (en) * | 2015-04-01 | 2015-08-05 | 中石化上海工程有限公司 | Bubbling reactor and use thereof |
| CN106607004A (en) * | 2015-10-21 | 2017-05-03 | 中国石油化工股份有限公司 | Circulation mixer and application thereof |
| CN108261988A (en) * | 2018-03-30 | 2018-07-10 | 中国海洋石油集团有限公司 | A kind of gas distributor and the system comprising the gas distributor |
-
2003
- 2003-01-30 CN CN 03233076 patent/CN2604434Y/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101811930B (en) * | 2009-02-19 | 2013-04-03 | 中国石油化工股份有限公司 | Selective hydrogenation method for phenylacetylene in phenylacetylene-containing styrene material flow |
| CN101885678A (en) * | 2010-07-05 | 2010-11-17 | 兖矿国泰化工有限公司 | Reaction equipment for synthesizing ethylic acid by low-pressure methanol carbonylation of methanol |
| CN101885678B (en) * | 2010-07-05 | 2013-03-13 | 兖矿国泰化工有限公司 | Reaction equipment for synthesizing ethylic acid by low-pressure methanol carbonylation of methanol |
| CN104028177A (en) * | 2013-03-06 | 2014-09-10 | 中石化上海工程有限公司 | Method for reinforcing mixing effect of hydraulic reaction apparatus |
| CN104815593A (en) * | 2015-04-01 | 2015-08-05 | 中石化上海工程有限公司 | Bubbling reactor and use thereof |
| CN106607004A (en) * | 2015-10-21 | 2017-05-03 | 中国石油化工股份有限公司 | Circulation mixer and application thereof |
| CN108261988A (en) * | 2018-03-30 | 2018-07-10 | 中国海洋石油集团有限公司 | A kind of gas distributor and the system comprising the gas distributor |
| CN108261988B (en) * | 2018-03-30 | 2021-06-04 | 中国海洋石油集团有限公司 | Gas distributor and system comprising same |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203196620U (en) | Reactor for producing methyl formate through carbonylation | |
| CN2604434Y (en) | Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid | |
| WO2011022349A1 (en) | Gravity flow tubular photobioreactor and photobioreactor farm | |
| CN202379802U (en) | Air lift type underwater aeration device based on high pressure air pump system | |
| CN109368824A (en) | Efficient jet aerator | |
| CN213644075U (en) | Microbubble generator and hydrocarbon oil hydrogenation reactor | |
| EP0008856B1 (en) | Apparatus and process for dissolution of gases in liquid | |
| CN2918407Y (en) | Multi-pipe jetting type oxygen aerator | |
| CN209143857U (en) | A kind of multi-spiral formula aeration tank | |
| CN201626961U (en) | Air distribution device | |
| CN200996011Y (en) | External circulating-current reactor of double-nozzle air-extracting | |
| CN201519551U (en) | Smoke gas desulfurization absorption tower with combined tower kettle liquid phase mixing system | |
| CN1136146C (en) | Integrated equipment and process for hydrogen antiraquinone oxidation and H2O2 extraction in producing H2O2 | |
| CN209155820U (en) | Efficient hybrid reaction slot | |
| CN208436628U (en) | Underneath type supplies jet stream and regenerates integrated desulfurization device | |
| CN208542016U (en) | Overhead supplies jet stream and regenerates integrated desulfurization device | |
| CN211936257U (en) | Induced air sprayer for 7-dehydrocholesterol production | |
| CN2747217Y (en) | Aerobic-anaerobic waste water treatment reactor | |
| CN100358617C (en) | Gas-water mixing device | |
| CN2665135Y (en) | Fermentation jar highly effective aeration diversion tube | |
| CN216149699U (en) | Glycolic acid preparation facilities of methyl glycolate hydrolysis method | |
| CN206692426U (en) | A kind of rotary mixing type gas explosion device | |
| CN219765352U (en) | membrane reactor | |
| CN214915911U (en) | Formic acid reactor | |
| CN219615250U (en) | Absorption tower for preparing refined sulfuric acid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SOUTHWEST RESEARCH + DESIGN INSTITUTE OF CHEMICAL Free format text: FORMER NAME: SOUTHWEST RESEARCH + DESIGN INSTITUTE OF CHEMICAL INDUSTRY |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 445 box 610255, South Airport Road, Sichuan, Chengdu, Chengdu Patentee after: Southwest Chemical Research & Design Institute Co., Ltd. Address before: 445 box 610255, South Airport Road, Sichuan, Chengdu, Chengdu Patentee before: Xinan Chemical Research & Design Inst. |
|
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Serra nice (Nanjing) Chemical Co., Ltd. Assignor: Southwest Chemical Research & Design Institute Co., Ltd. Contract record no.: 2013990000015 Denomination of utility model: Bubble tower converter for technology of methyl alcohol low pressure liquid phase carbonyl synthesizing acetic acid Granted publication date: 20040225 License type: Exclusive License Record date: 20130114 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20130130 Granted publication date: 20040225 |