CN108398040A - Rotary heat exchanger - Google Patents
Rotary heat exchanger Download PDFInfo
- Publication number
- CN108398040A CN108398040A CN201810411467.3A CN201810411467A CN108398040A CN 108398040 A CN108398040 A CN 108398040A CN 201810411467 A CN201810411467 A CN 201810411467A CN 108398040 A CN108398040 A CN 108398040A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- inner cylinder
- interlayer
- cylinder
- big
- 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.)
- Granted
Links
- 239000011229 interlayer Substances 0.000 claims abstract description 27
- 230000007246 mechanism Effects 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 23
- 229910052573 porcelain Inorganic materials 0.000 claims description 15
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 10
- 229910052719 titanium Inorganic materials 0.000 claims description 10
- 239000010936 titanium Substances 0.000 claims description 10
- 239000013055 pulp slurry Substances 0.000 claims description 3
- 235000010599 Verbascum thapsus Nutrition 0.000 claims description 2
- 244000178289 Verbascum thapsus Species 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D11/00—Heat-exchange apparatus employing moving conduits
- F28D11/02—Heat-exchange apparatus employing moving conduits the movement being rotary, e.g. performed by a drum or roller
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Paper (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention discloses a kind of rotary heat exchangers, including rack（1）, cylinder（2）And driving mechanism（5）, cylinder（2）Both ends feed end is respectively set（3）And discharge end（4）, the cylinder（2）Including shell（6）And inner cylinder（7）, inner cylinder（7）Respectively with feed end（3）And discharge end（4）The reaction mass delivery pipe of end（9）It is connected, shell（6）And inner cylinder（7）Between constitute interlayer（8）, interlayer（8）Respectively and feed end（3）And discharge end（4）On ore pulp pipe（10）It is connected；The inner cylinder（7）It is interior to be in charge of equipped with the axially disposed multiple heat exchange being circumferentially distributed（11）, which is in charge of（11）Both ends pass through endless tube respectively（12）With feed end（3）And discharge end（4）The heat exchanger tube at place（13）It is connected.The rotary heat exchanger of the present invention is simple in structure, it is full-featured, can improve production efficiency, therefore suitable for promoting the use of.
Description
Technical field
The present invention relates to a kind of fields such as energy environment protection, smelting, oil, chemical industry, printing and dyeing, pharmacy, food of can be used in
Rotary heat exchanger.
Background technology
The structure of existing rotary heat exchanger is single, can not provide various materials respectively while enter the interior progress of different cavities instead
It should exchange heat.
Invention content
In response to the problems existing in the prior art, the purpose of the present invention is to provide one kind can be while conveying various materials
It can carry out one-to-many or many-one reacting replacing heat rotary heat exchanger.
The purpose of the present invention is what is solved by the following technical programs：
A kind of rotary heat exchanger includes the driving mechanism of rack, the cylinder and driving cylinder rotation that can be rotated in rack, cylinder
Feed end and discharge end is respectively set in the both ends of body, it is characterised in that：The cylinder includes shell and inner cylinder, inner cylinder respectively with
Feed end is connected with the reaction mass delivery pipe of discharge end end, constitutes interlayer between shell and inner cylinder, interlayer respectively and into
Material end is connected with the ore pulp pipe on discharge end；The axially disposed multiple heat exchange being circumferentially distributed point are equipped in the inner cylinder
Pipe, the both ends which is in charge of are connected by endless tube with the heat exchanger tube at feed end and discharge end respectively.
The inner cylinder is made of the expansion joint of titanium plate and connection titanium plate.
Using the spacing between support orifice plate restriction shell and inner cylinder in the interlayer；And support plate is equipped in inner cylinder.
Being equipped in the inner cylinder and interlayer prevents the porcelain ball of material fouling, and the both ends of inner cylinder are equipped with can limit porcelain ball
The porous plate of motion range, the aperture minimum value on porous plate are less than the diameter of porcelain ball.
The all big conical head of the feed end and discharge end and feed end is additionally provided with fine taper end socket, the conelet of feed end
One end of shape end socket is connected with reaction mass delivery pipe and its other end is connected with the small bore end of big conical head, discharge end
The small bore end of big conical head be directly connected with reaction mass delivery pipe, the big nose end of big conical head is connected with shell
It connects, a conically shaped is equipped in the inner cavity of big conical head, the outer wall of conically shaped constitutes one with the inner wall of big conical head and is connected to
The conical cavity of interlayer, which is connected with ore pulp pipe enables ore pulp to enter in interlayer；The big conical head it is big
It is equipped with endless tube on the inside of nose end, the endless tube is connected with being in charge of across the heat exchanger tube of conical cavity and the heat exchange in inner cylinder respectively
It is logical.
One end of the conically shaped is fixed on the small bore end of big conical head and the other end of conically shaped is connected with inner cylinder
It connects.
Multiple porcelain balls that can prevent pulp slurry fouling in conical cavity are distributed in the conical cavity of the input end；It is described
The shovelling plate that multiple driving materials are advanced all is distributed on the inner wall of big conical head and the inner wall of conically shaped of outlet end.
The heat exchanger tube is symmetricly set on the both sides of reaction mass delivery pipe.
Ore pulp pipe on the big conical head is symmetricly set on the both sides of reaction mass delivery pipe.
The shell is also provided symmetrically the ore pulp pipe in reaction mass delivery pipe both sides, and the ore pulp pipe directly with
Interlayer is connected.
The present invention has the following advantages compared with prior art：
The present invention is by the setting of fine taper end socket, big conical head and heat exchanger tube, endless tube, ore pulp pipe with conical cavity, for rotation
Heat exchanger provides three kinds of material disengaging ports so that three kinds of materials, which can enter in rotary heat exchanger react, to be changed
Heat；And setting with inner cylinder is in charge of by interlayer, heat exchange so that three kinds of materials are taken their own roads, and the anti-of three kinds of materials can be carried out
Answer heat transfer process, and the inner cylinder being made up of the expansion joint of titanium plate and connection titanium plate so that inner cylinder has one when by hot stretched
Fixed stroke；Additionally by the setting of porcelain ball, fouling of the material in interlayer, inner cylinder and conical cavity is avoided, eliminates fouling
The influence of heat exchanging and material conveying；The rotary heat exchanger is simple in structure, it is full-featured, production efficiency can be improved, therefore suitable for pushing away
It is wide to use.
Description of the drawings
Attached drawing 1 is the structural schematic diagram of the rotary heat exchanger of the present invention.
Wherein：1-rack；2-cylinders；3-feed ends；4-discharge ends；5-driving mechanisms；6-shells；7-inner cylinders；
8-interlayers；9-reaction mass delivery pipes；10-ore pulp pipes；11-heat exchange are in charge of；12-endless tubes；13-heat exchanger tubes；14-is swollen
Swollen section；15-support orifice plates；16-support plates；17-porcelain balls；18-porous plates；19-fine taper end sockets；20-big taper envelopes
Head；21-conically shapeds；22-conical cavities.
Specific implementation mode
The present invention is further illustrated with embodiment below in conjunction with the accompanying drawings.
As shown in Figure 1：A kind of rotary heat exchanger, including rack 1, the cylinder 2 that can be rotated in rack 1 and driving cylinder
Feed end 3 and discharge end 4 is respectively set in the both ends of the driving mechanism 5 of 2 rotations, cylinder 2, and middle cylinder body 2 includes shell 6 and inner cylinder
7, inner cylinder 7 is made of the expansion joint 14 of titanium plate and connection titanium plate, the reactant with 4 end of feed end 3 and discharge end respectively of inner cylinder 7
Material conveying tube 9 is connected, and interlayer 8 is constituted between shell 6 and inner cylinder 7, and interlayer 8 is interior using support orifice plate 15 restriction shell 6 and interior
It is equipped with support plate 16 in spacing and inner cylinder 7 between cylinder 7；Interlayer 8 respectively with 10 phase of ore pulp pipe on feed end 3 and discharge end 4
Connection；It is in charge of 11 equipped with the axially disposed multiple heat exchange being circumferentially distributed in inner cylinder 7, which is in charge of 11 both ends difference
It is connected with the heat exchanger tube 13 at feed end 3 and discharge end 4 by endless tube 12.Being equipped in inner cylinder 7 and interlayer 8 prevents material knot
The porcelain ball 17 of dirt, and the both ends of inner cylinder 7 are equipped with the porous plate 18 that can limit 17 motion range of porcelain ball, the aperture on porous plate 18
Minimum value is less than the diameter of porcelain ball 17.
On the basis of above structure, feed end 3 and all big conical head 20 of discharge end 4 and feed end 3 are additionally provided with conelet
One end of shape end socket 19, the fine taper end socket 19 of feed end 3 is connected with reaction mass delivery pipe 9 and its other end and big taper
The small bore end of end socket 20 is connected, the small bore end of the big conical head 20 of discharge end 4 is directly connected with reaction mass delivery pipe 9
Logical, the big nose end of big conical head 20 is connected with shell 7, and a conically shaped 21, cone are equipped in the inner cavity of big conical head 20
One end of shape cylinder 21 is fixed on the small bore end of big conical head 20 and the other end of conically shaped 21 is connected with inner cylinder 7, therefore taper
The outer wall of cylinder 21 constitutes a conical cavity 22 for being connected to interlayer 8, the conical cavity 22 and ore pulp pipe 10 with the inner wall of big conical head 20
It is connected and ore pulp is entered in interlayer 8；Be equipped with endless tube 12 on the inside of the big nose end of big conical head 20, endless tube 12 respectively with
It is in charge of 11 with the heat exchange in inner cylinder 7 across the heat exchanger tube 13 of conical cavity 22 to be connected.Divide in the conical cavity 22 of input end 3
It is furnished with multiple porcelain balls 17 that can prevent pulp slurry fouling in conical cavity 22；And the big conical head 20 of the outlet end 4
The shovelling plate that multiple driving materials are advanced all is distributed on the inner wall of inner wall and conically shaped 2.In addition heat exchanger tube 13 is symmetricly set on instead
Answer the both sides of material delivery pipe 9；Ore pulp pipe 10 on big conical head 20 is symmetricly set on the both sides of reaction mass delivery pipe 9,
Also be provided symmetrically the ore pulp pipe 10 in 9 both sides of reaction mass delivery pipe in shell 6 simultaneously, and the ore pulp pipe 10 directly with folder
Layer 8 is connected.
The present invention passes through fine taper end socket 19, the big conical head 20 with conical cavity 22 and heat exchanger tube 13, endless tube 12, ore pulp
The setting of pipe 10 provides three kinds of materials for rotary heat exchanger and passes in and out port so that three kinds of materials can enter rotating heat transfer
Reacting replacing heat is carried out in device；And it is in charge of the setting of 11 and inner cylinder 7 by interlayer 8, heat exchange so that three kinds of materials are taken their own roads, energy
Enough carry out the reacting replacing heat process of three kinds of materials, and the inner cylinder 7 being made up of the expansion joint 14 of titanium plate and connection titanium plate so that interior
Cylinder 7 is when by hot stretched with certain stroke；Additionally by the setting of porcelain ball 17, material is avoided in interlayer 8, inner cylinder 7
With the fouling in conical cavity 22, the influence of fouling heat exchanging and material conveying is eliminated；The rotary heat exchanger is simple in structure, function is complete
Face can improve production efficiency, therefore suitable for promoting the use of.
Above example is merely illustrative of the invention's technical idea, and protection scope of the present invention cannot be limited with this, every
According to technological thought proposed by the present invention, any change done on the basis of technical solution each falls within the scope of the present invention
Within；The technology that the present invention is not directed to can be realized by the prior art.
Claims (10)
1. a kind of rotary heat exchanger, including rack（1）, can be in rack（1）The cylinder of upper rotation（2）With driving cylinder（2）Rotation
The driving mechanism turned（5）, cylinder（2）Both ends feed end is respectively set（3）And discharge end（4）, it is characterised in that：The cylinder
Body（2）Including shell（6）And inner cylinder（7）, inner cylinder（7）Respectively with feed end（3）And discharge end（4）The reaction mass of end conveys
Pipe（9）It is connected, shell（6）And inner cylinder（7）Between constitute interlayer（8）, interlayer（8）Respectively and feed end（3）And discharge end（4）
On ore pulp pipe（10）It is connected；The inner cylinder（7）It is interior to be in charge of equipped with the axially disposed multiple heat exchange being circumferentially distributed（11）,
The heat exchange is in charge of（11）Both ends pass through endless tube respectively（12）With feed end（3）And discharge end（4）The heat exchanger tube at place（13）It is connected
It is logical.
2. rotary heat exchanger according to claim 1, it is characterised in that：The inner cylinder（7）By titanium plate and connection titanium plate
Expansion joint（14）It constitutes.
3. rotary heat exchanger according to claim 1, it is characterised in that：The interlayer（8）It is interior to use support orifice plate
（15）Limit shell（6）And inner cylinder（7）Between spacing；And inner cylinder（7）It is interior to be equipped with support plate（16）.
4. rotary heat exchanger according to claim 1, it is characterised in that：The inner cylinder（7）And interlayer（8）Interior be equipped with is prevented
The only porcelain ball of material fouling（17）, and inner cylinder（7）Both ends be equipped with can limit porcelain ball（17）The porous plate of motion range（18）,
Porous plate（18）On aperture minimum value be less than porcelain ball（17）Diameter.
5. rotary heat exchanger according to claim 1, it is characterised in that：The feed end（3）And discharge end（4）It is all big
Conical head（20）And feed end（3）It is additionally provided with fine taper end socket（19）, feed end（3）Fine taper end socket（19）One end with
Reaction mass delivery pipe（9）It is connected and its other end and big conical head（20）Small bore end be connected, discharge end（4）It is big
Conical head（20）Small bore end directly with reaction mass delivery pipe（9）It is connected, big conical head（20）Big nose end with it is outer
Shell（7）It is connected, in big conical head（20）Inner cavity in be equipped with a conically shaped（21）, conically shaped（21）Outer wall and big taper
End socket（20）Inner wall constitute one connection interlayer（8）Conical cavity（22）, the conical cavity（22）With ore pulp pipe（10）Being connected makes
Interlayer can be entered by obtaining ore pulp（8）It is interior；The big conical head（20）Big nose end on the inside of be equipped with endless tube（12）, the endless tube
（12）Respectively with across conical cavity（22）Heat exchanger tube（13）With positioned at inner cylinder（7）In heat exchange be in charge of（11）It is connected.
6. rotary heat exchanger according to claim 5, it is characterised in that：The conically shaped（21）One end be fixed on auger
Shape end socket（20）Small bore end and conically shaped（21）The other end and inner cylinder（7）It is connected.
7. rotary heat exchanger according to claim 5, it is characterised in that：The input end（3）Conical cavity（22）Interior point
Being furnished with multiple can prevent pulp slurry in conical cavity（22）The porcelain ball of middle fouling（17）；The outlet end（4）Big conical head
（20）Inner wall and conically shaped（21）Inner wall on be all distributed with it is multiple driving materials advance shovelling plates.
8. rotary heat exchanger according to claim 1 or 5, it is characterised in that：The heat exchanger tube（13）It is symmetricly set on
Reaction mass delivery pipe（9）Both sides.
9. rotary heat exchanger according to claim 5, it is characterised in that：The big conical head（20）On ore pulp pipe
（10）It is symmetricly set on reaction mass delivery pipe（9）Both sides.
10. rotary heat exchanger according to claim 9, it is characterised in that：The shell（6）Also it is provided symmetrically
Reaction mass delivery pipe（9）The ore pulp pipe of both sides（10）, and the ore pulp pipe（10）Directly and interlayer（8）It is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810411467.3A CN108398040B (en) | 2018-05-02 | 2018-05-02 | Rotary heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810411467.3A CN108398040B (en) | 2018-05-02 | 2018-05-02 | Rotary heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108398040A true CN108398040A (en) | 2018-08-14 |
| CN108398040B CN108398040B (en) | 2024-01-12 |
Family
ID=63101458
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810411467.3A Active CN108398040B (en) | 2018-05-02 | 2018-05-02 | Rotary heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108398040B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109141067A (en) * | 2018-09-20 | 2019-01-04 | 南通星球石墨设备有限公司 | A kind of methyl alcohol vaporizing device |
| WO2019140961A1 (en) * | 2018-01-16 | 2019-07-25 | 金川集团股份有限公司 | High-temperature reaction material heat energy recovery device |
| CN111059936A (en) * | 2019-12-26 | 2020-04-24 | 无锡华邦智能装备有限公司 | Shell and tube heat exchanger with uniform heat exchange |
| CN111141161A (en) * | 2018-11-06 | 2020-05-12 | 金川集团股份有限公司 | Heat exchanger for material heat exchange and heat energy recovery |
| WO2020093367A1 (en) * | 2018-11-06 | 2020-05-14 | 金川集团股份有限公司 | Production line used for extracting nickel and cobalt from laterite nickel ore and having anti-scaling function |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0962590A2 (en) * | 1998-06-02 | 1999-12-08 | MARQUIP, Inc. | Rotary steam joint and valve assembly |
| CN1857766A (en) * | 2005-04-30 | 2006-11-08 | 杭州林达化工技术工程有限公司 | Heat exchanging reactor |
| CN101773808A (en) * | 2007-10-19 | 2010-07-14 | 杭州林达化工技术工程有限公司 | Combined reaction device |
| CN201935609U (en) * | 2011-01-26 | 2011-08-17 | 中节能六合天融环保科技有限公司 | Helical fin cooler for cooling high-temperature powdery materials |
| CN202028388U (en) * | 2011-04-14 | 2011-11-09 | 焦作煤业（集团）合晶科技有限责任公司 | Main reactor |
| CN203719470U (en) * | 2014-02-28 | 2014-07-16 | 金川集团股份有限公司 | Gas cooler |
| CN204535492U (en) * | 2015-02-12 | 2015-08-05 | 自贡市德明电站锅炉有限公司 | A kind of delivery heat transfer device |
| CN105091634A (en) * | 2014-05-21 | 2015-11-25 | 航天长征化学工程股份有限公司 | Baffle rod type heat exchanger with built-in expansion joint |
| JP2015535826A (en) * | 2012-09-24 | 2015-12-17 | アーケマ・インコーポレイテッド | Shell and tube oxidation reactor with improved fouling resistance |
| US20160018170A1 (en) * | 2012-12-05 | 2016-01-21 | Tojo KAMINO, | Scrape-off type heat exchanger |
| CN105865227A (en) * | 2016-05-30 | 2016-08-17 | 东方电气集团东方锅炉股份有限公司 | Roller type slag cooler using molten salt as cooling medium |
| CN106595348A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | No-scaling fluidized bed heat exchanger |
| CN106732315A (en) * | 2016-12-27 | 2017-05-31 | 扬州惠通化工科技股份有限公司 | A kind of rotary drum heating and stirring device |
| CN206996611U (en) * | 2017-07-14 | 2018-02-13 | 江苏远方迪威尔设备科技有限公司 | Rotatable reactor |
| CN208505081U (en) * | 2018-05-02 | 2019-02-15 | 江苏远方迪威尔设备科技有限公司 | Rotary heat exchanger |
-
2018
- 2018-05-02 CN CN201810411467.3A patent/CN108398040B/en active Active
Patent Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0962590A2 (en) * | 1998-06-02 | 1999-12-08 | MARQUIP, Inc. | Rotary steam joint and valve assembly |
| CN1857766A (en) * | 2005-04-30 | 2006-11-08 | 杭州林达化工技术工程有限公司 | Heat exchanging reactor |
| CN101773808A (en) * | 2007-10-19 | 2010-07-14 | 杭州林达化工技术工程有限公司 | Combined reaction device |
| CN201935609U (en) * | 2011-01-26 | 2011-08-17 | 中节能六合天融环保科技有限公司 | Helical fin cooler for cooling high-temperature powdery materials |
| CN202028388U (en) * | 2011-04-14 | 2011-11-09 | 焦作煤业（集团）合晶科技有限责任公司 | Main reactor |
| JP2015535826A (en) * | 2012-09-24 | 2015-12-17 | アーケマ・インコーポレイテッド | Shell and tube oxidation reactor with improved fouling resistance |
| US20160018170A1 (en) * | 2012-12-05 | 2016-01-21 | Tojo KAMINO, | Scrape-off type heat exchanger |
| CN203719470U (en) * | 2014-02-28 | 2014-07-16 | 金川集团股份有限公司 | Gas cooler |
| CN105091634A (en) * | 2014-05-21 | 2015-11-25 | 航天长征化学工程股份有限公司 | Baffle rod type heat exchanger with built-in expansion joint |
| CN204535492U (en) * | 2015-02-12 | 2015-08-05 | 自贡市德明电站锅炉有限公司 | A kind of delivery heat transfer device |
| CN106595348A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | No-scaling fluidized bed heat exchanger |
| CN105865227A (en) * | 2016-05-30 | 2016-08-17 | 东方电气集团东方锅炉股份有限公司 | Roller type slag cooler using molten salt as cooling medium |
| CN106732315A (en) * | 2016-12-27 | 2017-05-31 | 扬州惠通化工科技股份有限公司 | A kind of rotary drum heating and stirring device |
| CN206996611U (en) * | 2017-07-14 | 2018-02-13 | 江苏远方迪威尔设备科技有限公司 | Rotatable reactor |
| CN208505081U (en) * | 2018-05-02 | 2019-02-15 | 江苏远方迪威尔设备科技有限公司 | Rotary heat exchanger |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019140961A1 (en) * | 2018-01-16 | 2019-07-25 | 金川集团股份有限公司 | High-temperature reaction material heat energy recovery device |
| CN109141067A (en) * | 2018-09-20 | 2019-01-04 | 南通星球石墨设备有限公司 | A kind of methyl alcohol vaporizing device |
| CN111141161A (en) * | 2018-11-06 | 2020-05-12 | 金川集团股份有限公司 | Heat exchanger for material heat exchange and heat energy recovery |
| WO2020093369A1 (en) * | 2018-11-06 | 2020-05-14 | 金川集团股份有限公司 | Heat exchanger for material heat exchange and heat energy recovery |
| WO2020093367A1 (en) * | 2018-11-06 | 2020-05-14 | 金川集团股份有限公司 | Production line used for extracting nickel and cobalt from laterite nickel ore and having anti-scaling function |
| CN111059936A (en) * | 2019-12-26 | 2020-04-24 | 无锡华邦智能装备有限公司 | Shell and tube heat exchanger with uniform heat exchange |
| CN111059936B (en) * | 2019-12-26 | 2021-06-08 | 无锡华邦智能装备有限公司 | Shell and tube heat exchanger with uniform heat exchange |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108398040B (en) | 2024-01-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108398040A (en) | Rotary heat exchanger | |
| CN103353246A (en) | Recuperative heat exchanger of powder | |
| CN208505081U (en) | Rotary heat exchanger | |
| CN201173664Y (en) | Double-temperature internal heating double cones vacuum drying machine | |
| CN206152685U (en) | Novel interchangeable thermal agitation axle and tubular reactor | |
| CN207630738U (en) | Print chill roll | |
| CN104711419B (en) | The cooling cylinder of reduced iron rotation drum type cooling machine | |
| CN103644722B (en) | Vertical material rolling dryer | |
| CN203964718U (en) | Rotating screw tubular type heat exchanger | |
| US2798693A (en) | Rotary heat exchangers | |
| CN104089502B (en) | Rotating screw tubular type heat exchanger | |
| CN205747861U (en) | Three dryness storehouses of heat pipe-type | |
| CN203249471U (en) | Rotating steam drier | |
| CN104864688B (en) | Large multi-tube diffusion airflow rotary dryer and drying method | |
| CN215209158U (en) | Phosphogypsum is calcined with preheating rotary kiln | |
| KR102301898B1 (en) | Indirect heating tube rotary dryer and drying method | |
| CN105843347B (en) | Bidirectional flow heat exchanger based on vibration induction | |
| CN207894257U (en) | Heat exchange shaft kiln | |
| CN209459405U (en) | A kind of kiln rotary cooling device | |
| CN107036466A (en) | Heat-exchanger rig | |
| WO2015156205A1 (en) | Horizontal rotary dryer | |
| CN208505068U (en) | A kind of tube structure of rotary heat exchanger | |
| US2504156A (en) | Drum | |
| CN207317597U (en) | Continuous spiral baffle plate and continuous spiral baffle plate heat exchanger with same | |
| CN214233964U (en) | Cracking cylinder, cracking equipment and cracking system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20231129 Address after: No. 18 Junzhi Road, Xinjie Street, Yixing City, Wuxi City, Jiangsu Province, China, 214206 Applicant after: Jiangsu Faraway Coating Environmental Protection Technology Co.,Ltd. Address before: 214206 Junzhi Road, huankeyuan, Yixing City, Wuxi City, Jiangsu Province Applicant before: JIANGSU YUANFANG DWELL PRESSURE VESSEL Co.,Ltd. |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant |