CN107185471A - High intensity reactor - Google Patents
High intensity reactor Download PDFInfo
- Publication number
- CN107185471A CN107185471A CN201710399138.7A CN201710399138A CN107185471A CN 107185471 A CN107185471 A CN 107185471A CN 201710399138 A CN201710399138 A CN 201710399138A CN 107185471 A CN107185471 A CN 107185471A
- Authority
- CN
- China
- Prior art keywords
- fixed
- capping
- high intensity
- kettle
- outer courage
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000011229 interlayer Substances 0.000 claims abstract description 21
- 238000012856 packing Methods 0.000 claims abstract description 19
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 238000007599 discharging Methods 0.000 claims abstract description 13
- 239000002131 composite material Substances 0.000 claims abstract description 12
- 239000010410 layer Substances 0.000 claims abstract description 9
- 229910000975 Carbon steel Inorganic materials 0.000 claims abstract description 6
- 239000010962 carbon steel Substances 0.000 claims abstract description 6
- 239000010935 stainless steel Substances 0.000 claims abstract description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 16
- 210000000232 gallbladder Anatomy 0.000 claims description 8
- 210000003205 muscle Anatomy 0.000 claims description 2
- 239000008141 laxative Substances 0.000 claims 1
- 230000002475 laxative effect Effects 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 7
- 239000000376 reactant Substances 0.000 description 6
- 239000000654 additive Substances 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000003905 agrochemical Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0073—Sealings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/04—Pressure vessels, e.g. autoclaves
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
This application discloses a kind of high intensity reactor.The high intensity reactor, including agitating device, capping and kettle, the capping is provided with upper flange close to one end of the kettle, the kettle is provided with lower flange close to one end of the capping, the capping is fixed on by the upper flange on the lower flange of the kettle, the capping is provided with automated packing mouthful, manual feeding port and stirring port, the agitating device passes through and is fixed on the stirring port, the outside feeding device of automated packing mouthful connection, the manual feeding port is provided with cover plate, the cover plate is switchable to be fixed on the manual feeding port, the kettle includes outer courage, inner bag and discharging opening, the outer courage is fixed on the inner bladder outer wall, interlayer is formed between the outer courage and inner bag, the inner bag is made of composite plate, the composite plate includes carbon steel base layer and stainless steel internal layer, the discharging opening, which runs through, is fixed on the inner bag bottom.This novel high-strength reactor is high pressure resistant and high temperature resistant, has a wide range of application.
Description
Technical field
The application is related to reactor technical field, more particularly to a kind of high intensity reactor.
Background technology
The broad understanding of reactor has the container physically or chemically reacted, is matched somebody with somebody by the structure design to container and parameter
Put, realize the mixture function of heating, evaporation, cooling and the low high speed of technological requirement.Reactor be widely used in oil, chemical industry,
Rubber, agricultural chemicals, dyestuff, medicine, food, for completing to vulcanize, nitrify, hydrogenate, hydrocarbonylation, polymerization, the pressure of the technical process such as condensation
Force container, such as reactor, reaction pot, decomposition pot, polymeric kettle.Reactor is combined reaction container, according to reaction condition pair
Reactor structure function and the design for configuring annex.Can be with higher automaticity from charging-reaction-discharging of beginning
Pre-set reactions steps are completed, to the weight such as the temperature in course of reaction, pressure, mechanics control, reactant/product concentration
Parameter is wanted to carry out strict regulation and control.It is made more than existing reactor of carbon steel, to be worth high pressure resistant, resistant to elevated temperatures reactor,
It can only be realized by increasing the thickness of reactor, it is too fat to move to often result in reactor structure, also increase manufacturing cost, and simple
Using stainless steel making, cost is also huge.So needing to propose to improve.
The content of the invention
It is an object of the invention to provide a kind of high intensity reactor, to overcome deficiency of the prior art.
To achieve the above object, the present invention provides following technical scheme：
The embodiment of the present application discloses a kind of high intensity reactor, including agitating device, capping and kettle, and the capping is leaned on
One end of the nearly kettle is provided with upper flange, and the kettle is provided with lower flange close to one end of the capping, and the capping passes through
The upper flange is fixed on the lower flange of the kettle, and the capping is provided with automated packing mouthful, manual feeding port and stirring
Mouthful, the agitating device passes through and is fixed on the stirring port, the outside feeding device of automated packing mouthful connection, described manual
Feeding port is provided with cover plate, and the cover plate is switchable to be fixed on the manual feeding port, and the kettle includes outer courage, inner bag and discharging
Mouthful, the outer courage is fixed on the inner bladder outer wall, is formed with interlayer between the outer courage and inner bag, the inner bag uses composite plate
It is made, the composite plate includes carbon steel base layer and stainless steel internal layer, the discharging opening, which runs through, is fixed on the inner bag bottom.
It is preferred that, in above-mentioned high intensity reactor, the stirring port, which runs through, is fixed on the capping, the stirring port
The cap central is arranged at, the automated packing mouthful and manual feeding port, which run through, is fixed on the capping.
It is preferred that, in above-mentioned high intensity reactor, the interlayer is connected with inlet and liquid outlet, the inlet
With liquid outlet through the outer courage is fixed on, the inlet is arranged at the outer courage close to one end of the lower flange, described
Liquid outlet, which runs through, is fixed on the outer courage close to one end of the discharging opening.
It is preferred that, in above-mentioned high intensity reactor, the interlayer is provided with tap hole close to one end of the liquid outlet,
The tap hole is arranged at the minimum point of the outer courage.
It is preferred that, in above-mentioned high intensity reactor, the tap hole is provided with plug.
It is preferred that, in above-mentioned high intensity reactor, spiral deflector is provided with the interlayer.
It is preferred that, in above-mentioned high intensity reactor, the inner bladder outer wall is provided with impingement baffle, and the impingement baffle is just to institute
State inlet.
It is preferred that, in above-mentioned high intensity reactor, the capping is at least provided with four hangers, and the hanger is equidistant
Array is arranged at the top of the capping.
It is preferred that, in above-mentioned high intensity reactor, the outer gall bladder wall is at least provided with four fixed supports, the fixation
The equidistant array of support is arranged at the outer gall bladder wall, and the fixed support is arranged at the outer courage close to the one of the lower flange
End.
It is preferred that, in above-mentioned high intensity reactor, the fixed support includes a bottom plate, at least two gussets and a company
Fishplate bar, the bottom plate is arc plate, and the radius of the bottom plate is identical with the radius of the outer gall bladder wall, and the bottom plate is fixed on institute
Outer gall bladder wall is stated, the gusset is individually fixed in the bottom plate, and the gusset is arranged in parallel, the gusset is along the outer courage
Axially arranged, the connecting plate is connected to the gusset bottom
Compared with prior art, the advantage of the invention is that：This novel high-strength reactor compact conformation, is provided with simultaneously
Automated packing mouthful and manual feeding port, after by automated packing mouthful addition main reactant, because indivedual auxiliary additives pair
The addition time requires, you can added by manual feeding port, additionally by the product of detection discharge outlet, if reaction is not
Thoroughly, it is possible to catalyst is added by manual feeding port and accelerates reaction process, and inner bag is made of composite plate, is just strengthened
The intensity of kettle, can with the wider array of reaction pressure of tolerance range and temperature.
Brief description of the drawings
, below will be to embodiment or existing in order to illustrate more clearly of the embodiment of the present application or technical scheme of the prior art
There is the accompanying drawing used required in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments described in application, for those of ordinary skill in the art, on the premise of not paying creative work,
Other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 show the structural representation of high intensity reactor in the specific embodiment of the invention.
Fig. 2 show the top view of high intensity reactor in the specific embodiment of the invention.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, detailed retouch is carried out to the technical scheme in the embodiment of the present invention
State, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.Based on the present invention
In embodiment, the every other implementation that those of ordinary skill in the art are obtained on the premise of creative work is not made
Example, belongs to the scope of protection of the invention.
Join shown in Fig. 1 and Fig. 2, the high intensity reactor in the present embodiment, including agitating device 10, capping 20 and kettle
30, capping 20 is provided with upper flange 21 close to one end of kettle 30, and kettle 30 is provided with lower flange 31, capping close to one end of capping 20
20 are fixed on the lower flange 31 of kettle 30 by upper flange 21, and capping 20 is provided with automated packing mouthful 22, manual feeding port 23
And stirring port 24, agitating device 10 passes through and is fixed on stirring port 24, the outside feeding device of the connection of automated packing mouthful 22, fills out manually
Material mouth 23 is provided with cover plate, and cover plate is switchable to be fixed on the manual feeding port 23, and kettle 30 includes outer courage 32, inner bag 33 and discharging
Mouth 34, outer courage 32 is fixed on the outer wall of inner bag 33, and interlayer 35 is formed between outer courage 32 and inner bag 33, and inner bag 33 uses composite plate system
Into composite plate includes carbon steel base layer and stainless steel internal layer, and discharging opening 34, which runs through, is fixed on the bottom of inner bag 33.
In the technical scheme, this novel high-strength reactor compact conformation, while being provided with automated packing mouthful and filling out manually
Material mouth, after by automated packing mouthful addition main reactant, because indivedual auxiliary additives are required to the addition time, you can
Added by manual feeding port, additionally by the product of detection discharge outlet, if reaction is not thorough, it is possible to by manual
Feeding port adds catalyst to accelerate reaction process, and inner bag is made of composite plate, just strengthens the intensity of kettle, Ke Yicheng
By the wider array of reaction pressure of scope and temperature, when basic unit's carbon steel thickness of composite plate is 25mm, stainless steel internal layer thickness is 3mm
When, kettle can bear 4.8MPa pressure and 200 DEG C of high temperature.
Further, stirring port 24 is arranged at the center of capping 20, automated packing through capping 20, stirring port 24 is fixed on
Mouth 22 and manual feeding port 23, which run through, is fixed on capping 20.
In the technical scheme, stirring port 24 is arranged at the center of capping 20 through capping 20, stirring port 24 is fixed on, it is ensured that
Stirring it is abundant, automated packing mouthfuls 22 and manual feeding port 23 are through being fixed on capping 20, automated packing mouthful 22 and manual filler
Mouth 23 is communicated in inside kettle.
Further, interlayer 35 is connected with inlet 351 and liquid outlet 352, and inlet 31 and liquid outlet 352 are through fixation
In outer courage 32, inlet 351 is arranged at outer courage 32 close to one end of lower flange 31, and liquid outlet 352 is leaned on through being fixed on outer courage 32
One end of nearly discharging opening 34.
In the technical scheme, interlayer 35 is connected with inlet 351 and liquid outlet 352, and inlet 31 and liquid outlet 352 run through
Outer courage 32 is fixed on, inlet 351 is arranged at outer courage 32 close to one end of lower flange 31, and liquid outlet 352, which runs through, is fixed on outer courage
32 close to one end of discharging opening 34, for the circulation of heat-conducting medium, in order to being attached internal reactant heating.
Further, interlayer 35 is provided with tap hole 353 close to one end of liquid outlet 352, and tap hole 353 is arranged at outer courage 32
Minimum point.
In the technical scheme, interlayer 35 is provided with tap hole 353 close to one end of liquid outlet 352, and tap hole 353 is arranged at outer
The minimum point of courage 32, without using when the medium of interlayer 35 can be completely vented.
Further, tap hole 353 is provided with plug.
In the technical scheme, tap hole 353 is provided with plug, during high intensity reactor use of the present invention, and plug is blocked up
In tap hole 353, interlayer 35 is confined space, flows through heating medium, is that reactant is heated in kettle, in high intensity of the present invention reaction
When kettle is without using process, plug is outwarded winding, residual heating medium in interlayer 35 is emptied.
Further, spiral deflector 354 is provided with interlayer 35.
In the technical scheme, be provided with that heating medium in spiral deflector 354, extension interlayer 35 flows through in interlayer 35 when
Between so that the heat entrained by heating medium is more fully utilized.
Further, the outer wall of inner bag 33 is provided with impingement baffle 331, and impingement baffle 331 is just to inlet 351.
In the technical scheme, the outer wall of inner bag 33 is provided with impingement baffle 331, and impingement baffle 331 just to inlet 351, uses process
In, heating medium constantly pours interlayer from inlet 351, in the process, the protection inner bag 33 of impingement baffle 331, it is to avoid long-term
Damaged using the inner bag caused.
Further, capping 20 is at least provided with four hangers 25, and the equidistant array of hanger 25 is arranged at the top of capping 20.
In the technical scheme, capping 20 is at least provided with four hangers 25, and the equidistant array of hanger 25 is arranged at capping 20
Top, the lifting of convenient capping 20.
Further, the outer outer wall of courage 32 is at least provided with four fixed supports 36, and the equidistant array of fixed support 36 is arranged at outer
The outer wall of courage 32, fixed support 36 is arranged at outer courage 32 close to one end of lower flange 31.
In the technical scheme, the outer outer wall of courage 32 is set at least provided with four fixed supports 36, the equidistant array of fixed support 36
The outer outer wall of courage 32 is placed in, fixed support 36 is arranged at outer courage 32 close to one end of lower flange 31, for fixed high intensity of the present invention
Reactor.
Further, fixed support 36 includes a bottom plate 361, at least two gussets 362 and a connecting plate 363, and bottom plate 361 is
Arc plate, the radius of bottom plate 361 is identical with the radius of the outer outer wall of courage 32, and bottom plate 361 is fixed on the outer outer wall of courage 32,362 points of gusset
Bottom plate 361 is not fixed on, gusset 362 is arranged in parallel, gusset 362 is axially arranged along outer courage 32, and connecting plate 363 is connected to muscle
The bottom of plate 362
In the technical scheme, fixed support 36 includes a bottom plate 361, at least two gussets 362 and a connecting plate 363, bottom
Plate 361 is arc plate, and the radius of bottom plate 361 is identical with the radius of the outer outer wall of courage 32 so that bottom plate 361 can fit in outer completely
Courage 32 so that fixed support connects more firm between kettle 30.
In summary, this novel high-strength reactor compact conformation, while automated packing mouthful and manual feeding port are provided with,
After by automated packing mouthful addition main reactant, because indivedual auxiliary additives are required to the addition time, you can pass through
Manual feeding port addition, additionally by the product of detection discharge outlet, if reaction is not thorough, it is possible to pass through manual filler
Mouth adds catalyst to accelerate reaction process, and inner bag is made of composite plate, just strengthens the intensity of kettle, can bear model
Enclose wider array of reaction pressure and temperature.
It should be noted that herein, such as first and second or the like relational terms are used merely to a reality
Body or operation make a distinction with another entity or operation, and not necessarily require or imply these entities or deposited between operating
In any this actual relation or order.Moreover, term " comprising ", "comprising" or its any other variant are intended to
Nonexcludability is included, so that process, method, article or equipment including a series of key elements not only will including those
Element, but also other key elements including being not expressly set out, or also include being this process, method, article or equipment
Intrinsic key element.In the absence of more restrictions, the key element limited by sentence "including a ...", it is not excluded that
Also there is other identical element in process, method, article or equipment including the key element.
Described above is only the embodiment of the application, it is noted that for the ordinary skill people of the art
For member, on the premise of the application principle is not departed from, some improvements and modifications can also be made, these improvements and modifications also should
It is considered as the protection domain of the application.
Claims (10)
1. a kind of high intensity reactor, it is characterised in that the high intensity reactor, including agitating device, capping and kettle, described
Capping is provided with upper flange close to one end of the kettle, and the kettle is provided with lower flange, the envelope close to one end of the capping
Lid is fixed on by the upper flange on the lower flange of the kettle, and the capping is provided with automated packing mouthful, manual feeding port
And stirring port, the agitating device passes through and is fixed on the stirring port, the outside feeding device of automated packing mouthful connection, institute
Manual feeding port is stated provided with cover plate, the cover plate is switchable to be fixed on the manual feeding port, and the kettle includes outer courage, inner bag
And discharging opening, the outer courage is fixed on the inner bladder outer wall, and interlayer is formed between the outer courage and inner bag, and the inner bag is used
Composite plate is made, and the composite plate includes carbon steel base layer and stainless steel internal layer, and the discharging opening, which runs through, is fixed on the inner bag bottom
Portion.
2. high intensity reactor according to claim 1, it is characterised in that：The stirring port, which runs through, is fixed on the envelope
Lid, the stirring port is arranged at the cap central, and the automated packing mouthful and manual feeding port, which run through, is fixed on the capping.
3. high intensity reactor according to claim 1, it is characterised in that：The interlayer is connected with inlet and goes out liquid
Mouthful, the inlet and liquid outlet are through the outer courage is fixed on, and the inlet is arranged at the outer courage close to the laxative remedy
Blue one end, the liquid outlet, which runs through, is fixed on the outer courage close to one end of the discharging opening.
4. high intensity reactor according to claim 3, it is characterised in that：The interlayer is close to one end of the liquid outlet
Provided with tap hole, the tap hole is arranged at the minimum point of the outer courage.
5. high intensity reactor according to claim 4, it is characterised in that：The tap hole is provided with plug.
6. high intensity reactor according to claim 1, it is characterised in that：Spiral deflector is provided with the interlayer.
7. high intensity reactor according to claim 3, it is characterised in that：The inner bladder outer wall is provided with impingement baffle, described
Impingement baffle is just to the inlet.
8. high intensity reactor according to claim 1, it is characterised in that：The capping is at least provided with four hangers, institute
The equidistant array of hanger is stated to be arranged at the top of the capping.
9. high intensity reactor according to claim 1, it is characterised in that：The outer gall bladder wall fixes branch at least provided with four
Frame, the equidistant array of fixed support is arranged at the outer gall bladder wall, and the fixed support is arranged at the outer courage close to institute
State one end of lower flange.
10. high intensity reactor according to claim 9, it is characterised in that：The fixed support includes a bottom plate, at least
Two gussets and a connecting plate, the bottom plate are arc plate, and the radius of the bottom plate is identical with the radius of the outer gall bladder wall, described
Bottom plate is fixed on the outer gall bladder wall, and the gusset is individually fixed in the bottom plate, and the gusset is arranged in parallel, the muscle
Plate is axially arranged along the outer courage, and the connecting plate is connected to the gusset bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710399138.7A CN107185471A (en) | 2017-05-31 | 2017-05-31 | High intensity reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710399138.7A CN107185471A (en) | 2017-05-31 | 2017-05-31 | High intensity reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107185471A true CN107185471A (en) | 2017-09-22 |
Family
ID=59876298
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710399138.7A Pending CN107185471A (en) | 2017-05-31 | 2017-05-31 | High intensity reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107185471A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173957A (en) * | 2018-08-24 | 2019-01-11 | 张家港市科华化工装备制造有限公司 | The fast-open type feed inlet of high-intensitive reaction kettle |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205323687U (en) * | 2016-01-05 | 2016-06-22 | 江苏七叶乳胶有限公司 | Reaction kettle feeding device |
| CN206121749U (en) * | 2016-10-25 | 2017-04-26 | 临沂中天环保科技有限公司 | Stainless steel reaction kettle |
| CN206184435U (en) * | 2016-11-11 | 2017-05-24 | 天津市长芦化工新材料有限公司 | Novel reation kettle of preparation perfluor propionyl fluoride |
| CN206746563U (en) * | 2017-05-31 | 2017-12-15 | 张家港市科华化工装备制造有限公司 | High intensity reactor |
-
2017
- 2017-05-31 CN CN201710399138.7A patent/CN107185471A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205323687U (en) * | 2016-01-05 | 2016-06-22 | 江苏七叶乳胶有限公司 | Reaction kettle feeding device |
| CN206121749U (en) * | 2016-10-25 | 2017-04-26 | 临沂中天环保科技有限公司 | Stainless steel reaction kettle |
| CN206184435U (en) * | 2016-11-11 | 2017-05-24 | 天津市长芦化工新材料有限公司 | Novel reation kettle of preparation perfluor propionyl fluoride |
| CN206746563U (en) * | 2017-05-31 | 2017-12-15 | 张家港市科华化工装备制造有限公司 | High intensity reactor |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173957A (en) * | 2018-08-24 | 2019-01-11 | 张家港市科华化工装备制造有限公司 | The fast-open type feed inlet of high-intensitive reaction kettle |
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| SE01 | Entry into force of request for substantive examination | ||
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| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170922 |
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| WD01 | Invention patent application deemed withdrawn after publication |