CN207562838U - A kind of Material Ratio System - Google Patents
A kind of Material Ratio System Download PDFInfo
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- CN207562838U CN207562838U CN201721645878.6U CN201721645878U CN207562838U CN 207562838 U CN207562838 U CN 207562838U CN 201721645878 U CN201721645878 U CN 201721645878U CN 207562838 U CN207562838 U CN 207562838U
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- mixer
- product pump
- storage device
- reaction unit
- value
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Abstract
The utility model provides a kind of Material Ratio System, belongs to material proportion technical field, including mixer, reaction unit, temperature sensor, PLC controller, material storage device, product pump and material pipe；Temperature sensor is arranged on reaction unit；Material storage device, product pump, mixer and reaction unit, are sequentially connected by material pipe；The signal output end of temperature sensor and the signal input part of PLC controller connect, and the signal input part of product pump and the signal output end of PLC controller connect, and material storage device is tangentially fed by material pipe into mixer.The utility model Material Ratio System, by using mixer, before material enters reaction unit, automatic uniform mixing preparation is carried out to the material of different calorific values according to the temperature in reaction unit, improve material proportion regulated efficiency, so that the temperature in reaction unit keeps stablizing, processing working efficiency is improved.
Description
Technical field
The utility model belongs to material proportion technical field, is to be related to a kind of Material Ratio System more specifically.
Background technology
Supercritical water oxidation method treatment technology is by the use of supercritical water as medium, under high-temperature and high-pressure conditions, by waste water
Or contained organic matter resolves into the simple nontoxic micromolecular compound such as water, carbon dioxide with oxygen in sewage.Faced due to super
Boundary's water oxidation treatment technology nearly reaches 100%, and in totally-enclosed shape to organic matter clearance rate contained in waste water or sewage
State organic matter is fully oxidized, non-secondary pollution, and therefore, technique is increasingly subject to the attention of people.
Supercritical water oxidation method treatment technology is carried out under 500 DEG C of temperature ＞, the high-temperature and high-pressure conditions of pressure ＞ 23Mpa
, material is directly filled with into reaction unit with pipeline and oxygen is reacted, generates high temperature and pressure.Because of waste liquid supplied materials calorific value not
Stablize, each proportioning process is complicated, can not uniformly mix, and reaction unit temperature change is big, and not easy to control, leads to reaction unit
Temperature modulation process time is long, influences the efficiency of waste water or sewage treatment works.
Utility model content
The purpose of this utility model is to provide a kind of Material Ratio System, before material enters reaction unit, according to
Temperature in reaction unit carries out automatic uniform mixing preparation to the material of different calorific values using mixer, solves reaction unit
Interior temperature change is big, manually matches the problem of specific efficiency is low.
To achieve the above object, the technical solution adopted in the utility model is：A kind of Material Ratio System is provided, including mixed
Clutch, reaction unit, temperature sensor, PLC controller, material storage device, product pump and material pipe；The temperature sensing
Device is arranged on the reaction unit；The material storage device, product pump, mixer and reaction unit, pass through the material
Pipeline is sequentially connected；The signal output end of the temperature sensor and the signal input part of PLC controller connect, and the material
The signal input part of pump is connect with the signal output end of the PLC controller, and the material storage device passes through the materail tube
Road is tangentially fed into the mixer.
Further, the material storage device include high heating value material storage device, middle calorific value material storage device and
Low heat value material storage device；The product pump includes high heating value product pump, middle calorific value product pump and low heat value product pump, described
High heating value material storage device, middle calorific value material storage device and low heat value material storage device pass through high heating value material respectively
Pump, middle calorific value product pump connect mixer with low heat value product pump.
Further, the high heating value product pump, middle calorific value product pump and low heat value product pump pass through high heating value object respectively
Pipe material, middle calorific value material pipe and low heat value material pipe are connect with mixer；
The middle calorific value material pipe realizes that material exports in the counterclockwise direction in mixer by being tangentially fed, described
High heating value material pipe, low heat value material pipe realize that material exports along clockwise direction in mixer by being tangentially fed.
Further, the mixer is cylindrical shape.
Further, the mixer diameter is more than the material pipe diameter.
Further, filter device is equipped between the mixer and the reaction unit.
Further, agitating device is equipped in the mixer.
The advantageous effect of air-conditioning system provided by the utility model is：Compared with prior art, the utility model material
Matching system, by using mixer, before material enters reaction unit, according to the temperature in reaction unit to different calorific values
Material carry out automatic uniform mixing preparation, material proportion regulated efficiency is improved, so that temperature in reaction unit is kept
Stablize, improve material processing working efficiency.
Description of the drawings
It, below will be to embodiment or the prior art in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
Attached drawing is briefly described needed in description, it should be apparent that, the accompanying drawings in the following description is only that this practicality is new
Some embodiments of type, for those of ordinary skill in the art, without having to pay creative labor, can be with
Other attached drawings are obtained according to these attached drawings.
Fig. 1 is the structure diagram of Material Ratio System that the utility model embodiment provides；
Fig. 2 is that high heating value material pipe, middle calorific value material pipe, low heat value material pipe connect with mixer and cut in Fig. 1
Face schematic diagram；
In figure：1st, high heating value material storage device, 2, middle calorific value material storage device, 3, low heat value material storage device,
4th, high heating value product pump, 5, middle calorific value product pump, 6, low heat value product pump, 7, mixer, 8, high heating value material pipe, 9, middle heat
It is worth material pipe, 10, low heat value material pipe, 11, filter device, 12, reaction unit, 13, temperature inductor.
Specific embodiment
In order to which technical problem to be solved in the utility model, technical solution and advantageous effect is more clearly understood, with
Lower combination accompanying drawings and embodiments, the present invention is further described in detail.It should be appreciated that specific reality described herein
It applies example to be only used to explain the utility model, is not used to limit the utility model.
It should be noted that when element is referred to as " being fixed on " or " being set to " another element, it can be directly another
On one element or it is connected on another element.When an element is known as " being connected to " another element, it can
To be directly to another element or be indirectly connected on another element.
It is to be appreciated that term " length ", " width ", " on ", " under ", "front", "rear", "left", "right", " vertical ",
The orientation or position relationship of the instructions such as " level ", " top ", " bottom " " interior ", " outer " are to be closed based on orientation shown in the drawings or position
System is for only for ease of the description present invention and simplifies description rather than instruction or imply that signified device or element must have
Specific orientation, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.
In addition, term " first ", " second " are only used for description purpose, and it is not intended that instruction or hint relative importance
Or the implicit quantity for indicating indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include one or more this feature.In the description of the present invention, " multiple " are meant that two or more,
Unless otherwise specifically defined.
It please refers to Fig.1 and Fig. 2, now Material Ratio System provided by the utility model is illustrated.
The Material Ratio System is deposited including mixer 7, reaction unit 12, temperature sensor 13, PLC controller, material
Storage device, product pump and material pipe；The temperature sensor 13 is arranged on the reaction unit 12；The material storage dress
It puts, product pump, mixer 7 and reaction unit 12, is sequentially connected by the material pipe；The signal of the temperature sensor 13
Output terminal and the signal input part of PLC controller connect, and the signal input part of the product pump and the letter of the PLC controller
The connection of number output terminal, the material storage device are tangentially fed by the material pipe into the mixer 7.
Material Ratio System provided in this embodiment, by using mixer 7, before material enters reaction unit 12,
Automatic uniform mixing preparation is carried out to the material of different calorific values according to the temperature in reaction unit 12, material storage device passes through object
Pipe material is tangentially fed into mixer 7, make different calorific values material be dispersed in a spiral manner along 7 inner wall of mixer it is mixed
In clutch 7, the full and uniform mixing preparation of material of different calorific values together, improves material proportion regulated efficiency, so that instead
The temperature in device 12 is answered to keep stablizing, improves material processing working efficiency.
Further, the material storage device includes high heating value material storage device 1, middle calorific value material storage device 2
With low heat value material storage device 3；The product pump includes high heating value product pump 4, middle calorific value product pump 5 and low heat value product pump
6, the high heating value material storage device 1, middle calorific value material storage device 2 and low heat value material storage device 3 pass through height respectively
Calorific value product pump 4, middle calorific value product pump 5 connect mixer with low heat value product pump 6.
Due to the material calorific value on-fixed value being transported in reaction unit 12, but the temperature in reaction unit 12 needs to control
Within a preset range.When the material being transported in reaction unit 12 makes temperature in reaction unit 12 by reacting the heat generated
During beyond preset temperature range, then need to convey the material of high heating value or low heat value into reaction unit 12 to reaction unit 12
Temperature be adjusted, so material storage device is provided with high heating value material storage device 1, middle calorific value material storage device 2
The material different with the storage calorific value of low heat value material storage device 3.High heating value material storage device 1, middle calorific value material storage dress
Put 2 and low heat value material storage device 3 respectively by high heating value product pump 4, middle calorific value product pump 5 and low heat value product pump 6, will
The material of different calorific values is delivered in mixer 7.
Details are as follows for specifically used process：First, calorific value product pump 5 in unlatching, will be in middle calorific value material storage device 2
Middle calorific value material is transported to by material pipe in mixer 7.Secondly, by the mixing of mixer 7, middle calorific value material is led to
Material pipe is crossed to be transported in reaction unit 12.Again, reaction is monitored by the temperature sensor 13 set on reaction unit 12
Temperature in device 12, and temperature signal is transmitted to PLC controller.Then, PLC control circuits are according to temperature sensor 12
Temperature information control material pump is turned on and off, and control enters the calorific value of material in reaction unit 12, so as to fill reaction
The temperature put in 12 is stablized.For example, the temperature range in default reaction unit 12 is 600 DEG C -650 DEG C, since material is reacting
It can be chemically reacted in device 12, so the temperature in reaction unit 12 can change.When 12 temperature of reaction unit is less than
At 600 DEG C, PLC controller control high heating value product pump 4 is opened, and high heating value material is conveyed to mixer 7；When 12 temperature of reaction unit
When degree is higher than 650 DEG C, PLC controller control low heat value product pump 6 is opened, and low heat value material is conveyed to mixer 7.It is filled with reaction
Rate of temperature change in 12 is put, the gradual load for adjusting product pump of PLC controller, i.e., rate of temperature change is big in reaction unit 12,
The load of product pump is big, and rate of temperature change is small in reaction unit 12, and the load of product pump is small.Finally, after the mixing of mixer 7
Material be delivered in reaction unit 12, ensure reaction unit 12 in temperature stablize.
Further, the high heating value product pump 4, middle calorific value product pump 5 and low heat value product pump 6 pass through high heating value respectively
Material pipe 8, middle calorific value material pipe 9 and low heat value material pipe 10 are connect with mixer；
The middle calorific value material pipe 9 realizes that material exports in the counterclockwise direction in mixer 7 by being tangentially fed, institute
State high heating value material pipe 8, low heat value material pipe 10 realizes material in mixer 7 along clockwise direction by being tangentially fed
Output.
Middle calorific value material pipe 9 is connect along the tangential direction in 7 section of mixer with the inner wall of mixer 7, middle calorific value material
Pipeline 9 realizes that material exports in the counterclockwise direction in mixer 7 by being tangentially fed, and enables middle calorific value material with counterclockwise
Direction, helical flow pattern are dispersed in 7 in mixer.To enable high heating value material or low heat value material and middle calorific value material
Enough uniformly to be mixed in mixer 7, high heating value material pipe 8, low heat value material pipe 10 realize that material exists by being tangentially fed
It is exported along clockwise direction in mixer 7, enables high heating value material, low heat value material in a clockwise direction, helical flow side
Formula is dispersed in mixer 7, and since high heating value material, low heat value material and middle calorific value material flow in mixer 7
Dynamic direction is opposite so that high heating value material, low heat value material are uniform during being flowed in mixer 7 with middle calorific value material
Mixing.The uniformity coefficient of different calorific value material mixing is improved, so as to improve material proportion regulated efficiency, is made in reaction unit 12
Temperature keeps stablizing.
Further, the mixer 7 is cylindrical shape.Mixer 7 is more advantageous to different calorific values for cylindrical shape
Material 7 inner wall of mixer formed spiral way be dispersed in mixer, the material of different calorific values is made adequately to be mixed.
Further, 7 diameter of mixer is more than the material pipe diameter.7 diameter of mixer is more than material pipe
It is anti-to ensure that there is mixer 7 sufficient space different calorific value materials to be made to enter after the interior progress of mixer 7 adequately mixes for diameter
Answer device 12.
Further, filter device 11 is equipped between the mixer 7 and the reaction unit 12.In mixer 7 and instead
It answers and filter device 11 is equipped between device 12, reaction unit 12 will be delivered to after the material that mixer 7 mixes is filtered
Interior, the impurity reduced in material is influenced caused by the reaction in reaction unit 12.
Further, agitating device is equipped in the mixer 7.Agitating device in mixer 7 can make different calorific values
Material be sufficiently mixed so that material obtains more adequately reacting in reaction unit 12, keep reaction unit 12 in temperature
Degree is stablized.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
All any modification, equivalent and improvement made within the spirit and principle of utility model etc., should be included in the utility model
Protection domain within.
Claims (7)
1. a kind of Material Ratio System, it is characterised in that：Including mixer, reaction unit, temperature sensor, PLC controller, object
Expect storage device, product pump and material pipe；The temperature sensor is arranged on the reaction unit；The material storage dress
It puts, product pump, mixer and reaction unit, is sequentially connected by the material pipe；The signal output of the temperature sensor
End is connect, and the signal input part of the product pump and the signal of the PLC controller are defeated with the signal input part of PLC controller
Outlet connects, and the material storage device is tangentially fed by the material pipe into the mixer.
2. Material Ratio System as described in claim 1, it is characterised in that：The material storage device includes high heating value material
Storage device, middle calorific value material storage device and low heat value material storage device；The product pump include high heating value product pump, in
Calorific value product pump and low heat value product pump, the high heating value material storage device, middle calorific value material storage device and low heat value object
Material storage device connects mixer by high heating value product pump, middle calorific value product pump with low heat value product pump respectively.
3. Material Ratio System as claimed in claim 2, it is characterised in that：The high heating value product pump, middle calorific value product pump
Connected respectively by high heating value material pipe, middle calorific value material pipe and low heat value material pipe and mixer with low heat value product pump
It connects；
The middle calorific value material pipe realizes that material exports in the counterclockwise direction in mixer by being tangentially fed, the high fever
Value material pipe, low heat value material pipe realize that material exports along clockwise direction in mixer by being tangentially fed.
4. Material Ratio System as described in claim 1, it is characterised in that：The mixer is cylindrical shape.
5. Material Ratio System as claimed in claim 4, it is characterised in that：The mixer diameter is more than the material pipe
Diameter.
6. Material Ratio System as described in claim 1, it is characterised in that：It is set between the mixer and the reaction unit
There is filter device.
7. Material Ratio System as described in claim 1, it is characterised in that：Agitating device is equipped in the mixer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721645878.6U CN207562838U (en) | 2017-11-30 | 2017-11-30 | A kind of Material Ratio System |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721645878.6U CN207562838U (en) | 2017-11-30 | 2017-11-30 | A kind of Material Ratio System |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207562838U true CN207562838U (en) | 2018-07-03 |
Family
ID=62689510
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721645878.6U Active CN207562838U (en) | 2017-11-30 | 2017-11-30 | A kind of Material Ratio System |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207562838U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111437762A (en) * | 2020-04-27 | 2020-07-24 | 廊坊新奥龙河环保科技有限公司 | Supercritical water oxidation device |
-
2017
- 2017-11-30 CN CN201721645878.6U patent/CN207562838U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111437762A (en) * | 2020-04-27 | 2020-07-24 | 廊坊新奥龙河环保科技有限公司 | Supercritical water oxidation device |
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