CN205073863U - Silicon tetrafluoride absorption tower - Google Patents
Silicon tetrafluoride absorption tower Download PDFInfo
- Publication number
- CN205073863U CN205073863U CN201520691147.XU CN201520691147U CN205073863U CN 205073863 U CN205073863 U CN 205073863U CN 201520691147 U CN201520691147 U CN 201520691147U CN 205073863 U CN205073863 U CN 205073863U
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- ocratation
- tower body
- absorption tower
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- outlet
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Abstract
The utility model provides a silicon tetrafluoride absorption tower, it includes tower body and circulating pump, the water inlet has been seted up at the top of tower body, the feed liquid import has been seted up on the upper portion of tower body, material liquid outlet has been seted up to the bottom of tower body, the intercommunication has silicon tetrafluoride charge -in pipeline on the tower body, the inside crisscross a plurality of sieves that are provided with of tower body, the last air intlet that has seted up of silicon tetrafluoride charge -in pipeline, the import and the export of circulating pump communicate through the circulating line respectively material liquid outlet with the feed liquid import, the feed liquid sampling outlet has been seted up on the circulating line. This silicon tetrafluoride absorption tower has the advantage that the design is scientific, the practicality is strong, production efficiency is high and production quality is reliable.
Description
Technical field
The utility model relates to a kind of absorption tower, specifically, relate to a kind of ocratation absorption tower.
Background technology
Ocratation is colourless irritative gas, and meet water generation pyrohydrolysis and generate white carbon, the chemical stability of white carbon is good, not easily decomposes, does not burn, specific area is large, electrical insulating property is strong by high temperature.Due to the characteristic of the facile hydrolysis of ocratation own, require the necessary dry and insulation of ocratation conveyance conduit, existing absorption tower structure simply causes feed concentration inadequate simultaneously, the drying cost of increase white carbon, how making feed concentration in absorption tower increase, is people's problem demanding prompt solutions.
In order to solve above Problems existing, people are seeking a kind of desirable technical solution always.
Summary of the invention
The purpose of this utility model is for the deficiencies in the prior art, thus a kind of design science is provided, practical, production efficiency is high and the reliable ocratation absorption tower of the quality of production.
To achieve these goals, the technical scheme that the utility model adopts is: a kind of ocratation absorption tower, it comprises tower body and circulating pump, the top of described tower body offers water inlet, the top of described tower body offers liquor inlet, the bottom of described tower body offers material liquid outlet, described tower body is communicated with ocratation feed pipe, described tower body alternate internal is provided with multiple sieve plate, described ocratation feed pipe offers air intlet, the import of described circulating pump is communicated with described material liquid outlet and described liquor inlet with outlet respectively by circulating line, described circulating line offers feed liquid sampling outlet.
Based on above-mentioned, described sieve plate is L shape sieve plate, and the bottom panel of described L shape sieve plate gathers air-vent.
Based on above-mentioned, described water inlet is arranged on the top of described liquor inlet.
Based on above-mentioned, described circulating line is positioned at described liquor inlet place and offers water supplement port.
Based on above-mentioned, described feed liquid sampling outlet place is provided with discharge valve.
Based on above-mentioned, described water supplement port place is provided with moisturizing valve.
The utility model hinge structure has substantive distinguishing features and progress, and specifically, the utility model comprises tower body and circulating pump, utilizes circulating pump to carry out circulation hydrolysis to feed liquid in tower body, increases the concentration of white carbon in the rear feed liquid of reaction with this; Furtherly described ocratation feed pipe offers air intlet, the clean ocratation that prevents of ocratation feed pipe is hydrolyzed blocking pipe in pipeline to utilize the air of high temperature drying to ensure; Feed liquid sampling outlet and water supplement port are set furtherly, carry out moisturizing and discharging white carbon suspension in time according to the concentration of white carbon in feed liquid; It has design science, practical, production efficiency is high and the reliable advantage of the quality of production.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below by detailed description of the invention, the technical solution of the utility model is described in further detail.
As shown in Figure 1, a kind of ocratation absorption tower, it comprises tower body 1 and circulating pump 2, this ocratation absorption tower can be hydrolyzed to ocratation and prepare white carbon, circulate owing to adopting circulating pump 2 to be hydrolyzed and ensure that the concentration of white carbon is high, reduce drying cost, enhance productivity.
The top of described tower body 1 offers water inlet 11, inputs clean water for being hydrolyzed ocratation with this; The top of described tower body 1 offers liquor inlet 13, and the ocratation after hydrolysis enters tower body again with this, is again hydrolyzed; The bottom of described tower body 1 offers material liquid outlet 12, and the ocratation of initial hydrolysis enters circulating pump 2 with this, is convenient to again be hydrolyzed; Described tower body 1 is communicated with ocratation feed pipe 3, carries ocratation with this; Described tower body 1 alternate internal is provided with multiple sieve plate 14, utilizes sieve plate 14 to slow down the decrease speed of the clean water entered in tower body, increases the time of contact with ocratation; Described ocratation feed pipe 3 offers air intlet 31, offering air intlet 31 for inputting high-temperature dry air, ensureing the dry cleansing of ocratation feed pipe 3 with this, prevent ocratation to be hydrolyzed in pipeline, and then blocking pipe; The import of described circulating pump 2 is communicated with described material liquid outlet 12 and described liquor inlet 13 with outlet respectively by circulating line, and the ocratation of initial hydrolysis again enters tower body 1 through this circulating pump 2 and is hydrolyzed, and improves the concentration of white carbon suspension with this; Described circulating line 2 offers feed liquid sampling outlet 41, judge that whether the concentration of white carbon suspension is suitable by sampling, according to sampled result, carry out discharge or add water or add silicon tetrafluoride gas, ensureing the normal work on whole ocratation absorption tower with this.
In the present embodiment, described sieve plate 14 is L shape sieve plates, and the bottom panel of described L shape sieve plate gathers air-vent, utilizes this air-vent to carry out the dirty of clean water, increases the reaction time with ocratation with this.
For the ease of adding water, described water inlet 11 is arranged on the top of described liquor inlet 13.Described circulating line is positioned at described liquor inlet 13 place and is provided with water supplement port 43, and the concentration according to white carbon suspension carries out in good time moisturizing, and described water supplement port 43 place is provided with moisturizing valve 44 simultaneously, ensures the timely and accurate of moisturizing.
For the ease of taking out white carbon suspension, described feed liquid sampling outlet 41 place is provided with discharge valve 42, is convenient to the rate of outflow controlling white carbon suspension.
Finally should be noted that: above embodiment is only in order to illustrate that the technical solution of the utility model is not intended to limit; Although be described in detail the utility model with reference to preferred embodiment, those of ordinary skill in the field have been to be understood that: still can modify to detailed description of the invention of the present utility model or carry out equivalent replacement to portion of techniques feature; And not departing from the spirit of technical solutions of the utility model, it all should be encompassed in the middle of the technical scheme scope of the utility model request protection.
Claims (6)
1. an ocratation absorption tower, it is characterized in that: it comprises tower body and circulating pump, the top of described tower body offers water inlet, the top of described tower body offers liquor inlet, the bottom of described tower body offers material liquid outlet, described tower body is communicated with ocratation feed pipe, described tower body alternate internal is provided with multiple sieve plate, described ocratation feed pipe offers air intlet, the import of described circulating pump is communicated with described material liquid outlet and described liquor inlet with outlet respectively by circulating line, described circulating line offers feed liquid sampling outlet.
2. ocratation absorption tower according to claim 1, is characterized in that: described sieve plate is L shape sieve plate, and the bottom panel of described L shape sieve plate gathers air-vent.
3. ocratation absorption tower according to claim 1 and 2, is characterized in that: described water inlet is arranged on the top of described liquor inlet.
4. ocratation absorption tower according to claim 3, is characterized in that: described circulating line is positioned at described liquor inlet place and offers water supplement port.
5. ocratation absorption tower according to claim 1, is characterized in that: described feed liquid sampling outlet place is provided with discharge valve.
6. ocratation absorption tower according to claim 4, is characterized in that: described water supplement port place is provided with moisturizing valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520691147.XU CN205073863U (en) | 2015-09-09 | 2015-09-09 | Silicon tetrafluoride absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520691147.XU CN205073863U (en) | 2015-09-09 | 2015-09-09 | Silicon tetrafluoride absorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205073863U true CN205073863U (en) | 2016-03-09 |
Family
ID=55426304
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520691147.XU Expired - Fee Related CN205073863U (en) | 2015-09-09 | 2015-09-09 | Silicon tetrafluoride absorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205073863U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106799126A (en) * | 2017-03-19 | 2017-06-06 | 刘荣甫 | Device of the ammonia process of desulfurization energy-conservation more than one times |
-
2015
- 2015-09-09 CN CN201520691147.XU patent/CN205073863U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106799126A (en) * | 2017-03-19 | 2017-06-06 | 刘荣甫 | Device of the ammonia process of desulfurization energy-conservation more than one times |
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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 |
Granted publication date: 20160309 Termination date: 20210909 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |