CN109590095A - A kind of high-pressure jet breaking method - Google Patents
A kind of high-pressure jet breaking method Download PDFInfo
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- CN109590095A CN109590095A CN201811463687.7A CN201811463687A CN109590095A CN 109590095 A CN109590095 A CN 109590095A CN 201811463687 A CN201811463687 A CN 201811463687A CN 109590095 A CN109590095 A CN 109590095A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
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- Food Science & Technology (AREA)
- Disintegrating Or Milling (AREA)
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Abstract
The present invention relates to a kind of high-pressure jet breaking method using high-pressure jet spray head, it is provided with elastomeric element between the jet stream flow path features and sealing cover of the high-pressure jet spray head, jet stream flow path features are fixed with shell.In addition, the space for accommodating elastomeric element forms cushion chamber.The cushion chamber that the present invention designs can reduce pressure oscillation, improve crushing effect, reduce the particle diameter distribution of material.Furthermore it is possible to simplify the assembly of high-pressure jet spray head, damage of the jet stream flow path features in assembly is prevented；It can use the pressure of high-pressure pump generation, the automatic sealing realized between jet stream flow path features and shell；The expansion for the realization production capacity that can be convenient；Impact of the pressure oscillation for jet stream flow path features is reduced simultaneously, reduces the risk of its damage.
Description
Technical field
The invention belongs to crushing technology fields, are particularly applied to the jet mill technology of wet pulverizing processing.
Background technique
The principle that high-pressure jet crushes is different from traditional smashing and grinding equipment.By the thick slurry of corase grinding first in high injection
It is forced into operating pressure in stream mill, then, cellular structure of the thick slurry Jing Guo special designing after pressurization, at this point, thick slurry is in duct
Interior carry out flow at high speed, it is real under high shear, head-on collision and cavitation effect that the particle in thick slurry generates during flow at high speed
Existing dispersion and fining.High-pressure jet crushing technology can be carried out applying in fields such as food, drug, daily use chemicals, coating.Especially exist
Food processing field, skin slag, seed and the fibre composition of food material can also be broken refinement in the process, and reaching can be equal
The state of even suspension.Under conditions of high-pressure jet, other than the particle in slurry can be further crushed, food component
Molecular conformation and electrification situation can also change, so that the texture state of slurries can also occur significantly to change.This makes
The mouthfeel of beverage is obtained while getting a promotion, stability is also significantly improved, and can reduce making for emulsifier stabilizer
With.
The core component that high-pressure jet crushes is high-pressure jet spray head.High-pressure jet spray head mainly by jet stream flow path features and
The external shell composition for accommodating jet stream flow path features, discloses in the documents such as U.S. Patent application US4533254A.Existing
In technology, high-pressure jet spray head in the prior art, the inlet of jet stream flow path features directly with the pipeline that connect high-pressure pump
Docking.Since high-pressure pump uses the form of plunger pump, while piston reciprocation movement is to liquid pressing, there are impulse waves for pressure
It is dynamic.Pressure oscillation meeting is so that flow velocity of the material in jet stream flow path features fluctuates, to influence the effect crushed, increases object
The particle diameter distribution of material.In addition, pulse fluctuation can also generate biggish impact on jet stream flow path features, so that jet stream runner
Also the risk of damage is had on component.
On the other hand, external shell both ends are usually provided with the sealing cover structure that can be fastened, sealing cover and jet stream runner
It is directly contacted between component, in fastening, realizes the positioning to jet stream flow path features, and high densification is realized by the end face of contact
Envelope.But in fastening assembly, since the fastening force of application is larger, be easy to be broken jet stream flow path features, so that assembly
Failure.In addition, this structure is easy to accomplish for single jet stream flow path features, but when carrying out equipment capacity amplification, need
Same equipment has multiple high-pressure jet spray heads, and such structure is difficult to and assembles.This makes existing high pressure
Jet mill plant capacity is smaller, can only be applied mostly in laboratory scale, can not be raw in large-scale industrialization
It is applied in production.
Summary of the invention
In order to solve the above-mentioned technical problem, the high-pressure jet spray head that the present invention applies in for high-pressure jet breaking method
Structure redesigned, specific technical solution is as follows:
A kind of high-pressure jet breaking method, it is characterised in that jet mill is carried out in high-pressure jet grinding device, it is described
High-pressure jet grinding device includes high-pressure jet spray head or high-pressure jet Nozzle At The Ingot Mold group, and thick slurry raw material to be comminuted is forced into work
After pressure, jet mill is realized by high-pressure jet spray head or high-pressure jet Nozzle At The Ingot Mold group, the operating pressure is not less than
60MPa, the high-pressure jet spray head include shell 1, jet stream flow path features 2, elastomeric element 3, the sealing cover 4, sealing of tubular
Part 5, cushion chamber 6, in which: the sealing cover 4 is equipped with the first inlet 7；First is equipped at the tubular bottom center of the shell 1
Liquid outlet 8, the open end of the shell 1 are connect with the sealing cover 4；The seal member 5 is set to the sealing cover 4 and institute
State the junction of shell 1；The jet stream flow path features 2 are set to the intracavitary of the shell 1, towards 1 open end of shell
One side end face is equipped with the second inlet 9, and the other side end face center of the tubular bottom surface towards the shell 1 is equipped with the second liquid outlet
10；The elastomeric element 3 is set between the jet stream flow path features 2 and the sealing cover 4；The sealing cover 4 and the shell
Body 1 compresses the elastomeric element 3 when connecting, the compression of elastomeric element 3 generates elastic force and sets the jet stream flow path features 2
There is the end face of the second liquid outlet 10 to be in contact with the 1 tubular bottom surface of shell；The cushion chamber 6 is by the jet stream flow path features 2
The inner wall of a side end face and the shell 1 towards 1 open end of shell and the inner side end of the sealing cover 4 surround shape
At；The high-pressure jet Nozzle At The Ingot Mold group, including high-pressure jet spray head described in two or more.
Further, first inlet 7 is set on the wall to form the shell 1 of the cushion chamber 6.
Further, the internal diameter of the cushion chamber 6 is greater than the internal diameter of first inlet 7.
Further, the high-pressure jet spray head further includes sealing ring 11, and the sealing ring 11 is set to the jet stream
Between road component 2 and the shell 1.
Further, the sealing ring 11 includes two groups, wherein one group of side wall for being set to the jet stream flow path features 2 with
Between the shell 1, another group is set between the rear end face and the shell 1 of the jet stream flow path features 2.
Further, the elastomeric element 3 is selected from spring, elastic rubber.
Further, described to be connected as being threadedly coupled.
Further, the seal member 5 includes copper ring, polytetrafluoroethylene ring, rubber ring, PEEK ring.
Further, the shell of two or more high-pressure jet spray head is tied using whole in the high-pressure jet Nozzle At The Ingot Mold group
Structure processing obtains.
Further, the first inlet of each high-pressure jet spray head is all set in the shell to form the cushion chamber
On wall, and the cushion chamber of each high-pressure jet spray head is communicated with one another by the pipeline processed on shell.
Further, the high-pressure jet grinding device further includes high-pressure pump, feed liquor booster pump.
Further, the thick slurry raw material includes: food size, drug slurry.
Further, the food size includes: soybean slurry, nut slurry, cereal slurry, fruit slurry.
The beneficial effects of the present invention are: the present invention is redesigned by the structure to high-pressure jet spray head, is accommodated
The space of elastomeric element forms one cushion chamber.Preferably, the internal diameter of cushion chamber is greater than the internal diameter of the first inlet.In this way,
The cushion chamber makes the liquid material after pressurization have bigger volume space, can be effectively reduced pressure caused by plunger pump
Fluctuation can promote crushing effect in this way, reduce the grain of material so that the flow rate of liquid in jet stream flow path features is fluctuated and reduced
Diameter distribution.For the crushing effect of slurry to be comminuted, especially food size and drug slurry, has and be obviously improved work
With.
In addition, the structure of high-pressure jet spray head of the invention also solves other technologies existing for original high-pressure jet spray head
Problem:
Firstly, solving the problems, such as that jet stream flow path features are easily damaged in assembly.High injection according to the present invention
It flowing in spray head, elastomeric element is provided between jet stream flow path features and sealing cover, sealing cover compresses elastomeric element in fastening,
Elastomeric element compression generates elastic force and contacts the rear end face of jet stream flow path features with shell.In this way, in assembly, jet stream
Fastening force suffered by flow path features be it is controllable, avoid the excessive risk being damaged of fastening force.Secondly, solving high pressure
Fluid jet nozzle is easy the problem of revealing because of poorly sealed under high pressure.The present invention in a high voltage state, jet stream flow path features
Front end face by inlet end pressure and be in close contact rear end face and shell, realize the automatic-sealed under high pressure, simply
And it is effective.It is also provided with sealing ring between jet stream flow path features and shell, to further enhance sealing effect.Third solves
Existing high-pressure nozzle structure is difficult to the problem of amplifying production.High-pressure jet nozzle structure according to the present invention, can also be square
Just by multiple high-pressure jet spray heads, the high-pressure jet Nozzle At The Ingot Mold group for the formula that becomes one realizes that production capacity expands.It is whole in same
In body metal material, can process several can accommodate the cavity of jet stream flow path features, pass through processing between cushion chamber
Pipeline is connected, and then can realize amplification production by these cavitys of seal cap sealing.Simultaneously amplify the equipment of production with
The equipment of single high-pressure jet spray head independent pulverizing unit having the same, it is ensured that large scale equipment has phase with small device
Same crushing effect.4th, solve the problems, such as the jet stream runner parts damages as caused by pressure oscillation in application process.
Detailed description of the invention
Fig. 1 is the cross-sectional view of the high-pressure jet spray head in the embodiment of the present invention 1.1 it is shell, 2 is jet stream flow path features, 3
It is elastomeric element, 4 be sealing cover, 5 be sealing ring, 6 be cushion chamber, 7 be the first inlet, 8 be the first liquid outlet, 9 is second
Inlet, 10 are the second liquid outlets.
Fig. 2 is the cross-sectional view of the high-pressure jet spray head of the prior art in comparative example.201 it is shell, 202 is jet stream
Road component, 203 be seal nipple, 204 be fastening nut, 205 be sealing ring, 206 be inlet, 207 be liquid outlet.
Fig. 3 is the high-pressure jet Nozzle At The Ingot Mold group outline drawing in the embodiment of the present invention 2.302 it is integral housing, 304 is
Liquid mouth.
Fig. 4 is cross-sectional view of the high-pressure jet Nozzle At The Ingot Mold group along plane shown in dotted line of Fig. 3.301 be high-pressure jet spray head knot
Structure, 302 be integral housing, 303 be inlet, 304 be liquid outlet.
Fig. 5 is the cross-sectional view of the high-pressure jet spray head in the embodiment of the present invention 3.1 it is shell, 2 is jet stream flow path features, 3
It is elastomeric element, 4 be sealing cover, 5 be sealing ring, 6 be cushion chamber, 7 be the first inlet, 8 be the first liquid outlet, 9 is second
Inlet, 10 be the second liquid outlet, 11 be sealing ring.
Fig. 6 is that the high-pressure jet spray head of embodiment 1 and the high-pressure jet spray head of comparative example carry out soybean milk crushing
When, the particle diameter distribution comparison diagram of thin soya-bean milk after crushing.
Fig. 7 is that the high-pressure jet spray head of embodiment 1 and the high-pressure jet Nozzle At The Ingot Mold group of embodiment 2 carry out soybean milk crushing
When, the particle diameter distribution comparison diagram of thin soya-bean milk after crushing.
Fig. 8 is the flow diagram of high-pressure jet breaking method of the present invention.
Specific embodiment
Embodiment 1
A kind of high-pressure jet spray head, as shown in Figure 1, include Stainless Steel Shell 1, jet stream flow path features 2, stainless steel spring 3,
Sealing cover 4, sealing ring 5, cushion chamber 6, sealing cover 4 are equipped with the first inlet 7, and one end of shell 1 is equipped with the first liquid outlet 8, separately
One end and sealing cover 4 fasten, and sealing ring 5 is set between sealing cover 4 and shell 1；Jet stream flow path features 2 are set in shell 1,
One end is equipped with the second inlet 9, and the other end is equipped with the second liquid outlet 10；Elastomeric element 3 is set to jet stream flow path features 2 and sealing
Between lid 4, sealing cover 4 compresses elastomeric element 3 in fastening, and the compression of elastomeric element 3 generates elastic force for jet stream flow path features 2
It is fixed with shell 1；Cushion chamber 6 is by the front end face of jet stream flow path features 2 and the inner wall of shell 1 and the inner wall of sealing cover 4
It surrounds and is formed.
After material slurry is pressurizeed by high-pressure plunger pump, high-pressure jet spray head is entered by the first inlet 7, by cushion chamber 6
Afterwards, material slurry is entered in jet stream flow path features 2 by the second inlet 9 carries out jet mill, and smashed screened stock liquid successively passes through
It crosses the second liquid outlet 10 and the first liquid outlet 8 discharges.
It is tight as suffered by jet stream flow path features when carrying out the assembling of high-pressure jet spray head using the structure in the present embodiment
Gu power be it is controllable, jet stream flow path features be able to maintain it is intact, high-pressure jet spray head assembling yield rate be greater than 99%.
For the high-pressure jet spray head of the present embodiment when carrying out the crushing of soybean milk material, soya-bean milk thick first is by high-pressure plunger
Pump is forced into 120MPa, and after cushion chamber buffers, the pressure oscillation of soya-bean milk passes through jet stream flow path features powder within ± 2MPa
Thin soya-bean milk partial size d90 after broken is 41.5 microns, production capacity 450L/h.Simultaneously as pressure oscillation is smaller, pressure wave is reduced
The dynamic impact for jet stream flow path features, so that serviceability rate of the jet stream flow path features in long-time use is greater than 90%.It is intact
The calculation method of rate are as follows: flow occurs for total number 10, spray head or more different during 120MPa, 2000 hours production and applications
Often, i.e., flow sports ± 10% or more of normal discharge, then is determined as that the jet stream flow path features of the spray head are damaged, intact
The spray head number that rate=1- is damaged/total spray head number.
Comparative example
High-pressure jet spray head in the prior art, as shown in Fig. 2, being connect including shell 201, jet stream flow path features 202, sealing
First 203, fastening nut 204, sealing ring 205, inlet 206, liquid outlet 207.Jet stream flow path features are located in shell, both ends with
Seal nipple connects.Fastening nut pushes the seal nipple at both ends mobile to center and applies pressure, so that jet stream in fastening
Sealing is realized between the both ends and seal nipple of flow path features.
When being assembled using the structure in comparative example, due to jet stream flow path features applied by seal nipple it is tight
Solid pressure power is difficult to control, and fastening pressure is small, poorly sealed to leak, and fastening pressure crosses conference and makes jet stream flow path features
It is damaged, therefore the serviceability rate of work in-process jet stream flow path features is lower, the yield rate of high-pressure jet spray head assembling is only
80% or so.
For high-pressure jet spray head in the prior art when carrying out the crushing of soybean milk material, soya-bean milk thick first is by high-pressure column
Plug pump is forced into 120MPa, and the pressure oscillation of soya-bean milk passes through the smashed thin soya-bean milk partial size d90 of jet stream flow path features in ± 5MPa
It is 62.4 microns.When the high-pressure jet spray head of embodiment 1 and the high-pressure jet spray head of comparative example carry out soybean milk crushing,
The particle diameter distribution comparison diagram of thin soya-bean milk is as shown in Figure 6 after crushing.It can be seen that after the high-pressure jet spray head in embodiment 1 crushes
Soybean milk partial size d90 it is smaller, and the distribution of partial size is narrower.
Since pressure oscillation is larger, jet stream flow path features are by biggish impact, so that jet stream flow path features are in use
Also it is easy to be damaged, so that serviceability rate of the jet stream flow path features in long-time use is only 60% or so, so that this sets
It is standby to be difficult to be applied in the production of practical soya-bean milk.The calculation method of serviceability rate are as follows: total number 10, spray head or more, in 120MPa,
During 2000 hours production and applications, Traffic Anomaly occurs, i.e. flow sports ± 10% or more of normal discharge, then determines
It is damaged for the jet stream flow path features of the spray head, the spray head number that serviceability rate=1- is damaged/total spray head number.
Therefore, embodiment 1 simplifies the assembly of high-pressure jet spray head first, prevents jet stream compared with comparative example
Damage of the road component in assembly；Secondly, can use the pressure of high-pressure pump generation, it is automatic to realize jet stream flow path features and shell
Between sealing；Third, design have cushion chamber, can reduce pressure oscillation, improve crushing effect, reduce the partial size point of material
Cloth, while impact of the pressure oscillation for jet stream flow path features is reduced, reduce the risk of its damage.
Embodiment 2
A kind of high-pressure jet Nozzle At The Ingot Mold group, as shown in figure 3, wherein sectional view is as shown in Figure 4.Including high-pressure jet spray head knot
Structure 301, integral housing 302, inlet 303, liquid outlet 304.The wherein high pressure in high-pressure jet nozzle structure and embodiment 1
Fluid jet nozzle is almost the same, and only the position of the first inlet is changed to be set to the side for buffering cavity shell by being arranged on sealing cover
On wall, and cushion chamber is interconnected, unified to be fed by inlet 303.First liquid outlet of each high-pressure jet nozzle structure also phase
It is intercommunicated.
As it can be seen that embodiment 2 compared with comparative example, can easily realize the expansion of production capacity in same overall structure
Greatly.
For the high-pressure jet Nozzle At The Ingot Mold group of the present embodiment when carrying out the crushing of soybean milk material, soya-bean milk thick first is by high pressure
Plunger pump is forced into 120MPa, and after cushion chamber buffers, the pressure oscillation of soya-bean milk passes through jet stream flow path portion within ± 2MPa
The smashed thin soya-bean milk partial size d90 of part is 42.6 microns, production capacity 5400L/h.The high-pressure jet spray head and embodiment of embodiment 1
When 2 high-pressure jet Nozzle At The Ingot Mold group carries out soybean milk crushing, the particle diameter distribution comparison diagram of thin soya-bean milk is as shown in Figure 7 after crushing.
As it can be seen that embodiment 2 is compared with Example 1, production capacity while increasing 12 times, for soybean milk crushing effect with
Single high-pressure jet spray head is almost the same.
Embodiment 3
A kind of high-pressure jet spray head, as shown in Figure 5.It further include two groups of sealings compared with 1 mesohigh fluid jet nozzle of embodiment
Circle 11, wherein another group is set to jet stream flow path features 2 between one group of side wall for being set to jet stream flow path features 2 and shell 1
Between rear end face and shell 1.Sealing can be better achieved in the addition of two groups of sealing rings, while reducing for machining essence
The requirement of degree.
Embodiments of the present invention have been described in detail above, but also only to facilitate understand and explanation and illustrate, do not answer
It is considered as limitation of the present invention.The staff of any technical field can implement preferably according to the technique and scheme of the present invention
Case study on implementation, but it is all these change belong to scope of the presently claimed invention.
Claims (13)
1. a kind of high-pressure jet breaking method, it is characterised in that carry out jet mill, the height in high-pressure jet grinding device
Jet flow grinding device includes high-pressure jet spray head or high-pressure jet Nozzle At The Ingot Mold group, and thick slurry raw material to be comminuted is forced into work pressure
After power, jet mill is realized by high-pressure jet spray head or high-pressure jet Nozzle At The Ingot Mold group, the operating pressure is not less than 60MPa,
The high-pressure jet spray head includes shell (1), jet stream flow path features (2), elastomeric element (3), the sealing cover (4), sealing of tubular
Component (5), cushion chamber (6), in which:
The sealing cover (4) is equipped with the first inlet (7)；The first liquid outlet is equipped at the tubular bottom center of the shell (1)
(8), the open end of the shell (1) is connect with the sealing cover (4)；The seal member (5) is set to the sealing cover (4)
With the junction of the shell (1)；
The jet stream flow path features (2) are set to the intracavitary of the shell (1), the side towards the shell (1) open end
Face is equipped with the second inlet (9), and the other side end face center of the tubular bottom surface towards the shell (1) is equipped with the second liquid outlet
(10)；
The elastomeric element (3) is set between the jet stream flow path features (2) and the sealing cover (4)；The sealing cover (4)
Compress the elastomeric element (3) when connecting with the shell (1), elastomeric element (3) compression generates elastic force will be described
The end face that jet stream flow path features (2) are equipped with the second liquid outlet (10) is in contact with the shell (1) tubular bottom surface；
A side end face of the cushion chamber (6) by the jet stream flow path features (2) towards the shell (1) open end and the shell
The inner wall of body (1) and the inner side end of the sealing cover (4) surround to be formed；
The high-pressure jet Nozzle At The Ingot Mold group, including high-pressure jet spray head described in two or more.
2. high-pressure jet breaking method as described in claim 1, first inlet (7) is set to form the cushion chamber
(6) on the wall of the shell (1).
3. the internal diameter of high-pressure jet breaking method as described in claim 1, the cushion chamber (6) is greater than first inlet
(7) internal diameter.
4. high-pressure jet breaking method as described in claim 1, the high-pressure jet spray head further includes sealing ring (11), described
Sealing ring (11) is set between the jet stream flow path features (2) and the shell (1).
5. high-pressure jet breaking method as claimed in claim 4, the sealing ring (11) includes two groups, wherein one group is set to
Between the side wall and the shell (1) of the jet stream flow path features (2), another group is set to the jet stream flow path features (2)
Between rear end face and the shell (1).
6. high-pressure jet breaking method as described in claim 1, the elastomeric element (3) is selected from spring, elastic rubber.
7. high-pressure jet breaking method as described in claim 1, described to be connected as being threadedly coupled.
8. high-pressure jet breaking method as described in claim 1, the seal member (5) be selected from copper ring, polytetrafluoroethylene ring,
Rubber ring, PEEK ring.
9. high-pressure jet breaking method as described in claim 1, two or more high pressure in the high-pressure jet Nozzle At The Ingot Mold group
The shell of fluid jet nozzle is obtained using overall structure processing.
10. the first inlet of high-pressure jet breaking method as claimed in claim 9, each high-pressure jet spray head is all provided with
It is placed on the housing wall to form the cushion chamber, and the cushion chamber of each high-pressure jet spray head is by processing on shell
Pipeline communicates with one another.
11. high-pressure jet breaking method as described in claim 1, the high-pressure jet grinding device further include high-pressure pump, into
Liquid booster pump.
12. high-pressure jet breaking method as described in claim 1, the thick slurry raw material includes: food size, drug slurry.
13. high-pressure jet breaking method as claimed in claim 12, the food size include: soybean slurry, nut slurry,
Cereal slurry, fruit slurry.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201811463687.7A CN109590095A (en) | 2018-12-03 | 2018-12-03 | A kind of high-pressure jet breaking method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811463687.7A CN109590095A (en) | 2018-12-03 | 2018-12-03 | A kind of high-pressure jet breaking method |
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| CN109590095A true CN109590095A (en) | 2019-04-09 |
Family
ID=65960099
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| Application Number | Title | Priority Date | Filing Date |
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| CN201811463687.7A Pending CN109590095A (en) | 2018-12-03 | 2018-12-03 | A kind of high-pressure jet breaking method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117920422A (en) * | 2024-03-22 | 2024-04-26 | 北京三元食品股份有限公司 | Preparation method and equipment of kelp juice |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4533254A (en) * | 1981-04-17 | 1985-08-06 | Biotechnology Development Corporation | Apparatus for forming emulsions |
| CN205243755U (en) * | 2015-11-04 | 2016-05-18 | 浙江格美机电科技有限公司 | Jet pump subassembly |
| CN108247910A (en) * | 2018-03-26 | 2018-07-06 | 东莞市秉能橡胶有限公司 | A kind of ultra-high pressure water fluid jet injection apparatus |
| CN108636526A (en) * | 2018-04-24 | 2018-10-12 | 北京协同创新食品科技有限公司 | It is a kind of in supercriticality or using liquid gas as milling apparatus of decentralized medium and products thereof |
| CN109351443A (en) * | 2018-12-02 | 2019-02-19 | 北京协同创新食品科技有限公司 | A kind of high-pressure jet spray head and the high-pressure jet grinding device using the spray head |
-
2018
- 2018-12-03 CN CN201811463687.7A patent/CN109590095A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4533254A (en) * | 1981-04-17 | 1985-08-06 | Biotechnology Development Corporation | Apparatus for forming emulsions |
| CN205243755U (en) * | 2015-11-04 | 2016-05-18 | 浙江格美机电科技有限公司 | Jet pump subassembly |
| CN108247910A (en) * | 2018-03-26 | 2018-07-06 | 东莞市秉能橡胶有限公司 | A kind of ultra-high pressure water fluid jet injection apparatus |
| CN108636526A (en) * | 2018-04-24 | 2018-10-12 | 北京协同创新食品科技有限公司 | It is a kind of in supercriticality or using liquid gas as milling apparatus of decentralized medium and products thereof |
| CN109351443A (en) * | 2018-12-02 | 2019-02-19 | 北京协同创新食品科技有限公司 | A kind of high-pressure jet spray head and the high-pressure jet grinding device using the spray head |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117920422A (en) * | 2024-03-22 | 2024-04-26 | 北京三元食品股份有限公司 | Preparation method and equipment of kelp juice |
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