CN103432918A - Powder and liquid dissolution mixer - Google Patents
Powder and liquid dissolution mixer Download PDFInfo
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- CN103432918A CN103432918A CN2013103309493A CN201310330949A CN103432918A CN 103432918 A CN103432918 A CN 103432918A CN 2013103309493 A CN2013103309493 A CN 2013103309493A CN 201310330949 A CN201310330949 A CN 201310330949A CN 103432918 A CN103432918 A CN 103432918A
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Abstract
The invention relates to a powder and liquid dissolution mixer. A liquid infusion tube inputs liquid at constant pressure quantitatively; the liquid quickly enters an expansion mixing chamber through a left/right screw wing in a left/right rotation manner; a powder pneumatic conveying pipe is inserted into the middle of the expansion mixing chamber; powder is quantitatively input into a mouse cage mixing mechanism arranged in the expansion mixing chamber by a pneumatic force; and powder-containing gas in the liquid in the mouse cage mixing mechanism bubbles, writhes, and is dissolved and mixed in the liquid in a left/right rotation manner under double action of air-liquid kinetic energy. The mouse cage mixing mechanism herein exerts effects of retarding rotation and facilitating stirring, so that dissolution and mixing of the powder are accelerated. The dissolved liquid enters a second reducing pipeline containing a right/left screw wing, and the liquid forms baffling along a right/left screw line to be further dissolved, homogenized and mixed with the powder. The powder and liquid dissolution mixer overcomes the defects that the electric energy consumption of a mechanical or pneumatic stirring mode is high, and the mechanism maintenance quantity is high; no stirring is required; and the powder and liquid dissolution mixer is simple in structure, convenient to operate, and lower in implementation cost, and mixes more sufficiently and uniformly.
Description
Technical field
the present invention relates to a kind of blender, be specifically related to a kind of powder liquid and dissolve blender.
Background technology
at present, the powder liquid blender is widely used in the processing manufacturing industry fields such as medicine, chemical industry, food, synthetic fibers and environmental protection, and its purpose is powder is evenly mixed by a certain percentage with liquid, thereby forms the pulpous state product homogenized.For example, in the water treatment procedure of running water, the powder liquid blender can fully mix Powdered Activated Carbon with water, in order to improve the water treatment effect.
traditional hybrid technology is to complete in agitator, be to offer powder inlet on agitator, liquid-inlet and mixed material delivery outlet, the prior ratio according to a certain ratio of powder and liquid is transported in agitator, utilize agitator that powder-liquid is fully mixed, the agitator of the type mostly adopts machinery or strength agitating mode to carry out powder dissolving mixing, although this traditional mode mixed effect is better, but need to consume a large amount of electric energy, implementation cost is higher, and mechanism's maintenance capacity is relatively large.
Summary of the invention
for overcoming above-mentioned defect, purpose of the present invention is to provide a kind of overcome machinery or strength agitating mode consumption of electric energy is large, mechanism's maintenance capacity is large deficiency, need not stir, simple in structure easy to operate, the lower and powder liquid that mixes of implementation cost dissolves blender.
the objective of the invention is to be achieved through the following technical solutions:
a kind of powder liquid of the present invention dissolves blender, mainly comprise: the liquid delivery tube for delivery of preset pressure, predetermined amount liquid connected successively, be less than the first undergauge pipeline of described liquid delivery tube caliber, enlarge mixing chamber, be less than the second undergauge pipeline of described expansion mixing chamber caliber;
in described the first undergauge pipeline, be provided with for the conveying liquid body being formed to the left/right helical-blade wing of eddy flow; Be provided with in described expansion mixing chamber and be inserted in described expansion mixing chamber for delivery of the powder pneumatic carrier pipe containing powder gas, also comprise the corresponding described powder pneumatic carrier pipe mouth of pipe, the mouse cage mixed organization that the eddy flow liquid be mixed with containing powder gas is blocked, is uniformly mixed; In described the second undergauge pipeline, being provided with for the liquid formation eddy flow to being mixed with containing powder gas makes the powder dissolving be mixed in the right/left helical-blade wing in liquid.
as a modification of the present invention, described expansion mixing chamber is warp architecture, the input port of described expansion mixing chamber and described the first undergauge pipeline level connection joint, and the delivery outlet of described expansion mixing chamber vertically is connected with described the second undergauge pipeline.
on the basis of said structure, the input port of described expansion mixing chamber and delivery outlet are bell.
as a further improvement on the present invention, described powder pneumatic carrier pipe vertically inserts in described mouse cage mixed organization.
as of the present invention, further improve, described powder liquid dissolving blender also comprises with the second undergauge pipeline and being connected, the blinds separator for gas-liquid is separated.
preferred embodiment a kind of as the present invention, described powder liquid dissolves blender and also comprises the protective cover that is arranged on described blinds separator top, the gas that is mixed with liquid is isolated to liquid.
as another preferred embodiment of the present invention, described powder liquid dissolves blender and also comprises the liquid storing barrel that is arranged on described blinds separator bottom, the liquid of mixed dissolution powder is accepted.
wherein, the delivery outlet of described liquid delivery tube is bell.
a kind of powder liquid provided by the invention dissolves blender, liquid woven hose level pressure, quantitative infusion fluid, revolve shape with left/right and enter fast the expansion mixing chamber by dwindling left/right helical-blade wing in caliber the first undergauge pipeline, the powder pneumatic carrier pipe inserts and enlarges the mixing chamber middle part, by strength, powder is quantitatively inputted and is arranged in the mouse cage mixed organization enlarged in mixing chamber, in the mouse cage mixed organization in liquid containing powder gas under the gas liquid operated double acting, bubbling seethes the left/right rotation and dissolves and be mixed in liquid.The mouse cage mixed organization has played herein the retardance rotation and has been beneficial to the effect of stirring, makes the dissolving of powder mix quickening.Liquid after dissolving enters the second undergauge pipeline that contains right/left helical-blade wing, and liquid forms further dissolving of baffling, homogenizing, mixed powder along the right/left helix.This powder liquid dissolves blender and has overcome machinery or strength agitating mode consumption of electric energy is large, mechanism's maintenance capacity is large deficiency, need not stir, and simple in structure easy to operate, implementation cost is lower and mix more full and uniform.
the accompanying drawing explanation
for ease of explanation, the present invention is described in detail by following preferred embodiment and accompanying drawing.
fig. 1 is the structural representation that a kind of powder liquid of the present invention dissolves blender.
The specific embodiment
in order to make purpose of the present invention, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the present invention is further elaborated.Should be appreciated that specific embodiment described herein, only in order to explain the present invention, is not intended to limit the present invention.
please refer to Fig. 1, a kind of powder liquid of the present invention dissolves blender, mainly comprises: the conveying preset pressure be fixedly connected sequentially, the liquid delivery tube of predetermined amount liquid 1, the first undergauge pipeline 10 enlarge mixing chamber 4, the second undergauge pipelines 11, blinds separator 7.In this first undergauge pipeline 10, be provided with for the conveying liquid body being formed to the left/right helical-blade wing of eddy flow, in the second undergauge pipeline 11, also be provided with for the conveying liquid body being formed to the right/left helical-blade wing of eddy flow, these two parts are arranged to the helical-blade wing of different rotation directions, make the flow direction that enters expansion mixing chamber 4 contrary with the flow direction that enters the second undergauge pipeline 11, change rapidly flow direction, can more fully more uniformly powder be dissolved in liquid.In this specific embodiment, will be fixedly installed right-hand screw leaf wing 2 in the first undergauge pipeline 10, will be fixedly installed left-hand screw leaf wing 6 in the second undergauge pipeline 11.This right-hand screw leaf wing 2 and left-hand screw leaf wing 6 are undergauge speedup fine pitch helical-fin section.
wherein, the caliber of this liquid delivery tube 1 is greater than the first connected undergauge pipeline 10, and the delivery outlet of this liquid delivery tube 1 is bell, with the first undergauge pipeline 10 level connection joints.Change into small-bore pipeline the first undergauge pipeline 10 by large diameter pipeline liquid delivery tube 1 when liquid is carried, its flow velocity is accelerated, and the dextrorotation eddy flow that forms acceleration by right-hand screw leaf wing 2 enters in expansion mixing chamber 4.
this enlarges mixing chamber 4 is warp architecture, and flexibility is 90 degree.Input port and delivery outlet on it are bell, input port and the first undergauge pipeline 10 level connection joints, and delivery outlet vertically is connected with the second undergauge pipeline 11.These expansion mixing chamber 4 middle parts are fixedly installed mouse cage mixed organization 5, the top of this mouse cage mixed organization 5 vertically is provided with thinner powder pneumatic carrier pipe 3, by gas, quantitative powder is transported in mouse cage mixed organization 5 via powder pneumatic carrier pipe 3, containing the gas of quantitative powder in the liquid of dextrorotation eddy flow under the effect of current and the two kinetic energy of gas bubbling seethe dissolving, the effect that the mouse cage mixed organization 5 be fixedly installed has played herein the retardance rotation and stirred, make the mixed dissolution of powder in liquid more abundant.
the caliber of the second undergauge pipeline 11 is less than the caliber that enlarges mixing chamber 4, makes the flow rate of liquid that enters the second undergauge pipeline 11 accelerate.Solution after dissolving by the left-hand screw leaf wing 6 in the second undergauge pipeline 11, is provided with deflection plate on this left-hand screw leaf wing 6 downwards, and liquid will form laevorotatory stream further to powder dissolving, homogenizing, mixing along helix.
further, this powder liquid dissolve blender also comprise with the second undergauge pipeline 11 be fixedly connected with, for blinds separator 7 that gas-liquid is separated and be arranged on described blinds separator 7 tops, the gas that is mixed with liquid isolated to the protective cover 8 of liquid.Carry out gas and fluid separation applications from the liquid of the second undergauge pipeline 11 outputs via blinds separator 7, isolated liquid self-flowing is stored to liquid storing barrel 9.Uprising gas is inevitably carried a part of liquid secretly simultaneously, separated through the most of liquid of blinds separator 7, the gas of doping liquid is through again separating with protective cover 8 collisions, and isolated liquid self-flowing enters in liquid storing barrel 9, has effectively prevented from floating entrained liquids in excessive gas.
the foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any modifications of doing within the spirit and principles in the present invention, be equal to and replace and improvement etc., within all should being included in protection scope of the present invention.
Claims (8)
1. a powder liquid dissolves blender, it is characterized in that, mainly comprise: the liquid delivery tube for delivery of preset pressure, predetermined amount liquid connected successively, be less than the first undergauge pipeline of described liquid delivery tube caliber, enlarge mixing chamber, be less than the second undergauge pipeline of described expansion mixing chamber caliber;
In described the first undergauge pipeline, be provided with for the conveying liquid body being formed to the first helical-blade wing of eddy flow; Be provided with in described expansion mixing chamber and be inserted in described expansion mixing chamber for delivery of the powder pneumatic carrier pipe containing powder gas, also comprise the corresponding described powder pneumatic carrier pipe mouth of pipe, the mouse cage mixed organization that the eddy flow liquid be mixed with containing powder gas is blocked, is uniformly mixed; In described the second undergauge pipeline, being provided with for the liquid formation eddy flow to being mixed with containing powder gas makes the powder dissolving be mixed in the second helical-blade wing in liquid; Described the first helical-blade wing is contrary with the rotary orientation of the second helical-blade wing.
2.
a kind of powder liquid according to claim 1 dissolves blender, it is characterized in that, described expansion mixing chamber is warp architecture, the input port of described expansion mixing chamber and described the first undergauge pipeline level connection joint, and the delivery outlet of described expansion mixing chamber vertically is connected with described the second undergauge pipeline.
3.
a kind of powder liquid according to claim 2 dissolves blender, it is characterized in that, the input port of described expansion mixing chamber and delivery outlet are bell.
4.
a kind of powder liquid according to claim 1 dissolves blender, it is characterized in that, described powder pneumatic carrier pipe vertically inserts in described mouse cage mixed organization.
5.
dissolve blender according to the described a kind of powder liquid of claim 1-4 any one, it is characterized in that, described powder liquid dissolving blender also comprises with the second undergauge pipeline and being connected, the blinds separator for gas-liquid is separated.
6.
a kind of powder liquid according to claim 5 dissolves blender, it is characterized in that, described powder liquid dissolves blender and also comprises the protective cover that is arranged on described blinds separator top, the gas that is mixed with liquid is isolated to liquid.
7.
a kind of powder liquid according to claim 6 dissolves blender, it is characterized in that, described powder liquid dissolves blender and also comprises the liquid storing barrel that is arranged on described blinds separator bottom, the liquid of mixed dissolution powder is accepted.
8.
a kind of powder liquid according to claim 1 dissolves blender, it is characterized in that, the delivery outlet of described liquid delivery tube is bell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310330949.3A CN103432918B (en) | 2013-08-01 | 2013-08-01 | Powder and liquid dissolution mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310330949.3A CN103432918B (en) | 2013-08-01 | 2013-08-01 | Powder and liquid dissolution mixer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103432918A true CN103432918A (en) | 2013-12-11 |
| CN103432918B CN103432918B (en) | 2015-06-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310330949.3A Active CN103432918B (en) | 2013-08-01 | 2013-08-01 | Powder and liquid dissolution mixer |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020082607A1 (en) * | 2018-10-23 | 2020-04-30 | 常州机电职业技术学院 | Powder and liquid mixer |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4408890A (en) * | 1981-03-11 | 1983-10-11 | E. I. Du Pont De Nemours And Company | Pigment pre-blending mixhead attachment |
| CN1099795A (en) * | 1993-09-01 | 1995-03-08 | 赵柏松 | Internal and external double-circular current fermentation can |
| WO2000078466A1 (en) * | 1999-06-21 | 2000-12-28 | Fukuoka Prefectural Government | High-efficiency gas dissolving device |
| CN2827519Y (en) * | 2005-10-13 | 2006-10-18 | 南京红宝丽股份有限公司 | Combined mixer of strengthening mixing effect |
| CN201921642U (en) * | 2010-12-04 | 2011-08-10 | 金川集团有限公司 | Gas-liquid mixing device |
| CN203458988U (en) * | 2013-08-01 | 2014-03-05 | 中盐榆林盐化有限公司 | Powder and liquid dissolving mixer |
-
2013
- 2013-08-01 CN CN201310330949.3A patent/CN103432918B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4408890A (en) * | 1981-03-11 | 1983-10-11 | E. I. Du Pont De Nemours And Company | Pigment pre-blending mixhead attachment |
| CN1099795A (en) * | 1993-09-01 | 1995-03-08 | 赵柏松 | Internal and external double-circular current fermentation can |
| WO2000078466A1 (en) * | 1999-06-21 | 2000-12-28 | Fukuoka Prefectural Government | High-efficiency gas dissolving device |
| CN2827519Y (en) * | 2005-10-13 | 2006-10-18 | 南京红宝丽股份有限公司 | Combined mixer of strengthening mixing effect |
| CN201921642U (en) * | 2010-12-04 | 2011-08-10 | 金川集团有限公司 | Gas-liquid mixing device |
| CN203458988U (en) * | 2013-08-01 | 2014-03-05 | 中盐榆林盐化有限公司 | Powder and liquid dissolving mixer |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020082607A1 (en) * | 2018-10-23 | 2020-04-30 | 常州机电职业技术学院 | Powder and liquid mixer |
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| Publication number | Publication date |
|---|---|
| CN103432918B (en) | 2015-06-17 |
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