CN206408127U - Naphthalene water reducer production line is condensed process diluted material water supply installation - Google Patents
Naphthalene water reducer production line is condensed process diluted material water supply installation Download PDFInfo
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- CN206408127U CN206408127U CN201720104719.9U CN201720104719U CN206408127U CN 206408127 U CN206408127 U CN 206408127U CN 201720104719 U CN201720104719 U CN 201720104719U CN 206408127 U CN206408127 U CN 206408127U
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- waste gas
- mixing drum
- production line
- supply installation
- diluted material
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Abstract
Process diluted material water supply installation is condensed the utility model discloses a kind of naphthalene water reducer production line, including waste gas skirt, one end of waste gas skirt is stretched into sealing container, the other end is connected with mixing drum, the body of waste gas skirt, which is provided with inside degree adjustment valve, mixing drum, is provided with intake tunnel, and mixing drum is arranged right below apopore positioned at tapered portion opening, intake tunnel side wall offers in delivery hole, mixing tube inner chamber and is provided with deflection plate.The utility model utilizes meta-alkalescence water from the intake tunnel swash of wave, negative pressure is produced to draw the waste gas in sealing container, small part meta-alkalescence water enters the inner chamber of mixing drum from delivery hole simultaneously, and waste gas is fully absorbed through deflection plate, and absorbing liquid can be used directly during condensation process diluted material；In this way, air pollution problems inherent can be solved, the process problem of sewage can be solved again.
Description
Technical field
The utility model is related to chemical production equipment field, and in particular to a kind of naphthalene water reducer production line condensation process is dilute
Release material water supply installation.
Background technology
Naphthalene water reducer is a kind of using crude naphthalene as raw material, through throwing naphthalene, sulfonation, hydrolysis, condensation, neutralization, drying, packaging etc.
The high efficiency water reducing agent of technique productions, naphthalene water reducer as concrete additive, it is possible to reduce cement consumption, improve concrete
Quality.Naphthalene water reducer is that China uses the most maximum main additive kind of wide, consumption at present, with becoming that supply falls short of demand
Gesture, increasing enterprise starts to produce naphthalene water reducer.
The sulfonation of naphthalene water reducer production line and hydrolyzing process need to carry out in obturator, and obturator is in course of reaction
In can produce waste gas, waste gas is discharged after needing air extractor to draw and handle.On the other hand, condensation process diluted material needs to supply
Water installations are supplied water, and traditional water supply installation function is single, it is impossible to extract closed in sulfonation and hydrolyzing process out as power
Waste gas in device.
Utility model content
The purpose of this utility model is to overcome the above-mentioned problems in the prior art to give birth to there is provided a kind of naphthalene water reducer
Producing line is condensed process diluted material water supply installation, can extract useless in obturator in sulfonation and hydrolyzing process out as power
Gas, simplifies naphthalene water reducer production line.
To realize above-mentioned technical purpose and the technique effect, the utility model is to be achieved through the following technical solutions：
A kind of naphthalene water reducer production line is condensed process diluted material water supply installation, including waste gas skirt, the waste gas
One end of skirt is stretched into the sealing container of hydrolyzing process, and the other end is connected with mixing drum, the body of the waste gas skirt and set
There is the intake tunnel that the meta-alkalescence water swash of wave is provided with inside degree adjustment valve, the mixing drum, the lower end of the intake tunnel is set
There is the tapered portion with opening, the mixing drum is arranged right below apopore positioned at tapered portion opening, and the intake tunnel is close
The side wall of water inlet end is offered in delivery hole, the inner chamber between the mixing drum and intake tunnel provided with raising gas-liquid mixed efficiency
Deflection plate.
Further, the waste gas skirt is straight tube or Venturi tube.
Further, the deflection plate is in level or tilts down.
Further, uniform micropore on the plate body of the deflection plate.
Further, the mixing drum is structure as a whole with deflection plate, is made up of quartz material.
The beneficial effects of the utility model are：
The utility model, from the intake tunnel swash of wave, produces negative pressure to draw the waste gas in sealing container using meta-alkalescence water,
Small part meta-alkalescence water enters the inner chamber of mixing drum from delivery hole simultaneously, fully absorbs waste gas through deflection plate, absorbing liquid can be direct
Used during condensation process diluted material；In this way, air pollution problems inherent can be solved, sewage can be solved again
Process problem.
Certainly, implement any product of the present utility model to it is not absolutely required to while reaching all the above advantage.
Brief description of the drawings
In order to illustrate more clearly of the technical scheme of the utility model embodiment, make required for being described below to embodiment
Accompanying drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the present utility model,
For those of ordinary skill in the art, on the premise of not paying creative work, it can also be obtained according to these accompanying drawings
Other accompanying drawings.
Fig. 1 is structural representation of the present utility model；
In accompanying drawing, the list of parts representated by each label is as follows：
1- waste gas skirts, 2- sealing containers, 3- mixing drums, 4- degree adjustment valves, 5- intake tunnels, 6- apopores, 7- is led
Fluid apertures, 8- deflection plates.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The all other embodiment obtained, belongs to the scope of the utility model protection.
Refer to shown in Fig. 1, the present embodiment is a kind of naphthalene water reducer production line condensation process diluted material water supply dress
Put, including waste gas skirt 1, one end of waste gas skirt 1 is stretched into the sealing container 2 of hydrolyzing process, and the other end is connected with mixing drum
3, the body of waste gas skirt 1 is provided with degree adjustment valve 4, and the inside of mixing drum 3 is provided with the intake tunnel 5 of the meta-alkalescence water swash of wave,
The lower end of intake tunnel 5 is provided with the tapered portion with opening, and mixing drum 3 is arranged right below apopore 6 positioned at tapered portion opening, entered
Aquaporin-5 is offered in delivery hole 7, the inner chamber between mixing drum 3 and intake tunnel 5 provided with raising gas close to the side wall of water inlet end
The deflection plate 8 of liquid mixing efficiency.
Wherein, waste gas skirt 1 is straight tube or Venturi tube, and deflection plate 8 is in level or tilts down, the plate body of deflection plate 8
Upper uniform micropore.Mixing drum 3 is structure as a whole with deflection plate 8, is made up of quartz material.
One of the present embodiment has particular application as：In use, using meta-alkalescence water from the swash of wave of intake tunnel 5, it is most
The apopore 6 of meta-alkalescence water directly below is flowed out, and negative pressure is produced using Venturi effect during outflow, draws sealing container 2
In waste gas, least a portion of meta-alkalescence water from delivery hole 7 enter mixing drum 3 inner chamber, after fully absorbing waste gas through deflection plate 8 from
Apopore 6 is flowed out, and the absorbing liquid of outflow can be used directly during condensation process diluted material.In this way, can
Air pollution problems inherent is solved, the process problem of sewage can be solved again.
In the description of this specification, the description of reference term " one embodiment ", " example ", " specific example " etc. means
With reference to specific features, structure, material or the feature that the embodiment or example are described be contained in it is of the present utility model at least one
In embodiment or example.In this manual, the schematic representation of above-mentioned term is not necessarily referring to identical embodiment or
Example.Moreover, specific features, structure, material or the feature of description can be in any one or more embodiments or examples
In combine in an appropriate manner.
The utility model preferred embodiment disclosed above is only intended to help and illustrates the utility model.Preferred embodiment is simultaneously
There is no the details that detailed descriptionthe is all, it is only described embodiment that the utility model is not limited yet.Obviously, according to this theory
The content of bright book, can make many modifications and variations.This specification is chosen and specifically describes these embodiments, is in order to preferably
Principle of the present utility model and practical application are explained, so that skilled artisan can be best understood by and utilize this
Utility model.The utility model is only limited by claims and its four corner and equivalent.
Claims (5)
1. a kind of naphthalene water reducer production line is condensed process diluted material water supply installation, it is characterised in that：Including waste gas skirt,
One end of the waste gas skirt is stretched into the sealing container of hydrolyzing process, and the other end is connected with mixing drum, the waste gas skirt
Body is provided with the intake tunnel that the meta-alkalescence water swash of wave is provided with inside degree adjustment valve, the mixing drum, the intake tunnel
Lower end be provided with the tapered portion with opening, the mixing drum is located at tapered portion opening and is arranged right below apopore, the water inlet
Passage is offered in delivery hole, the inner chamber between the mixing drum and intake tunnel provided with raising gas-liquid close to the side wall of water inlet end
The deflection plate of mixing efficiency.
2. naphthalene water reducer production line according to claim 1 is condensed process diluted material water supply installation, its feature exists
In：The waste gas skirt is straight tube or Venturi tube.
3. naphthalene water reducer production line according to claim 1 is condensed process diluted material water supply installation, its feature exists
In：The deflection plate is in level or tilts down.
4. naphthalene water reducer production line according to claim 3 is condensed process diluted material water supply installation, its feature exists
In：Uniform micropore on the plate body of the deflection plate.
5. naphthalene water reducer production line according to claim 1 is condensed process diluted material water supply installation, its feature exists
In：The mixing drum is structure as a whole with deflection plate, is made up of quartz material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104719.9U CN206408127U (en) | 2017-01-24 | 2017-01-24 | Naphthalene water reducer production line is condensed process diluted material water supply installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104719.9U CN206408127U (en) | 2017-01-24 | 2017-01-24 | Naphthalene water reducer production line is condensed process diluted material water supply installation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206408127U true CN206408127U (en) | 2017-08-15 |
Family
ID=59557987
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720104719.9U Expired - Fee Related CN206408127U (en) | 2017-01-24 | 2017-01-24 | Naphthalene water reducer production line is condensed process diluted material water supply installation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206408127U (en) |
-
2017
- 2017-01-24 CN CN201720104719.9U patent/CN206408127U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170815 Termination date: 20220124 |