CN106512881B - One kind is used for oxidation barrel steam recovery tower - Google Patents
One kind is used for oxidation barrel steam recovery tower Download PDFInfo
- Publication number
- CN106512881B CN106512881B CN201611237561.9A CN201611237561A CN106512881B CN 106512881 B CN106512881 B CN 106512881B CN 201611237561 A CN201611237561 A CN 201611237561A CN 106512881 B CN106512881 B CN 106512881B
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- Prior art keywords
- tower
- tower body
- liquid storage
- packing
- gas
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- 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.)
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Classifications
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- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
-
- 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
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
- B01J4/002—Nozzle-type elements
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00182—Controlling or regulating processes controlling the level of reactants in the reactor vessel
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Gas Separation By Absorption (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
One kind is used for oxidation barrel steam recovery tower, it includes the tower body of a long tubular, is disposed with least three sections of packing layers being made of stainless steel ripple packing up and down in tower body, the water spray system of external water source is at least provided with above orlop packing layer；A gas-liquid separator is connected at the tower body upper end outlet, and outlet is connected to an air outlet pipe in the upper end of gas-liquid separator；The tower body bottom is provided with liquid storage cavity, and steam inlet tube is connected in the tower wall of liquid storage cylinder body ullage, and band is circumscribed with the lower part tower wall of liquid storage cavity and pumps hot reuse water pipe；Five sections of packing layers are disposed with up and down in the tower body, wherein being respectively arranged with water spray system above three sections of packing layers below, inspection chamber is both provided with the tower wall above every section of packing layer；It has the features such as structure composition is simple, and use is easy to operate, and vapor-liquid separation effect is good, and capacity usage ratio is high, and not only environmentally friendly but also energy-saving effect is obvious.
Description
Technical field
The present invention relates to a kind of steam recovery tower of iron oxide pigment production oxidation barrel, belong to Steam Recovery technology
Field.
Background technology
The oxidation barrel of iron oxide pigment production, raw iron oxide material is poured into from top, from bottom be sent into air and steam into
Row stirring reaction, the largely steam containing moisture content can be produced on the top of oxidation barrel, distilled water is called, how to efficiently use these
Steam and reuse, are related to environmentally friendly and energy saving；It is simply divided into heat by the method taken at present simply by steam-water separator
Water circulation, and hot gas etc.；Not only gas-liquid separation effect is poor, but also energy-saving effect unobvious.
The content of the invention
It is an object of the invention to overcome the shortcomings of the prior art, and it is simple to provide a kind of structure composition, uses behaviour
Facilitate, vapor-liquid separation effect is good, and capacity usage ratio is high, and not only environmentally friendly but also energy-saving effect is significantly used for oxidation barrel steam time
Receive tower.
The purpose of the present invention is come what is completed, one kind is used for oxidation barrel steam recovery tower, it is wrapped by following technical solution
The tower body of a long tubular is included, is disposed with least three sections of packing layers being made of stainless steel ripple packing up and down in tower body, extremely
Few water spray system that external water source is provided with above orlop packing layer；One is connected at the tower body upper end outlet
Gas-liquid separator, and outlet is connected to an air outlet pipe in the upper end of gas-liquid separator；The tower body bottom is provided with
Liquid storage cavity, steam inlet tube are connected in the tower wall of liquid storage cylinder body ullage, and band is circumscribed with the lower part tower wall of liquid storage cavity
Pump hot reuse water pipe.
As preferred：It is upper and lower in the tower body to be disposed with five sections of packing layers, wherein following three sections of packing layers is upper
Side is respectively arranged with water spray system, and inspection chamber is both provided with the tower wall above every section of packing layer；In the liquid storage cavity
In be configured with the liquid storage cylinder body fluid level controller to match with the pump to connect on hot reuse water pipe.
As preferred：It is described by the gas-liquid separator that one section of adapter connection is described at the tower body upper end outlet
Gas-liquid separator includes multiple uniformly distributed guide vanes installed in body entrance, is connected among the top of guide vane
One taper device, the body are cylindrical body, and the adapter and upper end outlet that lower end import connects the air outlet pipe caliber that connects are respectively less than
The barrel diameter of body, the maximum gauge on the taper device top in body are more than the half of barrel diameter.
The present invention is simple with structure composition, and use is easy to operate, and vapor-liquid separation effect is good, and capacity usage ratio is high, not only
The features such as environmentally friendly and energy-saving effect is obvious.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention.
Embodiment
Below in conjunction with attached drawing, the present invention will be described in detail：Shown in Fig. 1, one kind of the present invention is used for oxidation barrel
Steam recovery tower, it includes the tower body 1 of a long tubular, and be disposed with least three sections up and down in tower body 1 is filled out by stainless steel ripple
Expect the packing layer 2 of composition, the water spray system 3 of external water source, the water spray are at least installed above orlop packing layer 2
Device 3 can be made of the spray tube with spray orifice or nozzle, and this spray tube can be several rows of uniformly distributed or curve annulus group
Form；A gas-liquid separator 4 is connected at 1 upper end outlet of tower body, and outlet connects in the upper end of gas-liquid separator 4
There is an air outlet pipe 5；1 bottom of tower body is provided with liquid storage cavity 6, and steam inlet tube 7 is connected on 6 liquid level of liquid storage cavity
In the tower wall of side, the hot reuse water pipe 9 with pump 8 is circumscribed with the lower part tower wall of liquid storage cavity 6.
It is upper and lower in tower body 1 of the present invention to be disposed with five sections of packing layers 2 shown in figure, wherein following three sections are filled out
The top of the bed of material 2 is respectively arranged with water spray system 3, and inspection chamber 10 is both provided with the tower wall of every section of top of packing layer 2；
The liquid storage cylinder body fluid level controller 11 to match with the pump 8 that connects on hot reuse water pipe 9 is configured with the liquid storage cavity 6.
It is described by the gas-liquid separator 4 that one section of connection of adapter 12 is described at 1 upper end outlet of tower body of the present invention
Gas-liquid separator 4 includes multiple uniformly distributed guide vanes 13 installed in body entrance, among the top of guide vane 13
It is connected to a taper device 14, steam stream is hampered deceleration after by guide vane 13, realizes gas-liquid separation, and in uphill process
The obstruction on taper device inclined-plane, further reduction of speed, so as to further realize gas-liquid separation are run into again；The body 1 is tubular
Body, the connect caliber of air outlet pipe 5 of the adapter 12 and upper end outlet that lower end import connects is respectively less than the barrel diameter of body, in body
14 top of taper device maximum gauge be more than barrel diameter half.
Claims (2)
1. one kind is used for oxidation barrel steam recovery tower, it includes the tower body of a long tubular, is disposed with least up and down in tower body
Three sections of packing layers being made of stainless steel ripple packing, are at least provided with the water spray of external water source above orlop packing layer
Shower device；It is characterized in that a gas-liquid separator is connected at the tower body upper end outlet, and in the upper end of gas-liquid separator
Portion outlet is connected to an air outlet pipe；The tower body bottom is provided with liquid storage cavity, and steam inlet tube is connected to liquid storage cavity
In the tower wall of ullage, band is circumscribed with the lower part tower wall of liquid storage cavity and pumps hot reuse water pipe；
Included at the tower body upper end outlet by the gas-liquid separator that one section of adapter connection is described, the gas-liquid separator
Installed in multiple uniformly distributed guide vanes of body entrance, a taper device is connected among the top of guide vane, it is described
Body be cylindrical body, the adapter and upper end outlet that lower end import connects connect air outlet pipe caliber be respectively less than body cylinder it is straight
Footpath, the maximum gauge on the taper device top in body are more than the half of barrel diameter.
2. according to claim 1 be used for oxidation barrel steam recovery tower, it is characterised in that in the tower body up and down successively
Five sections of packing layers are provided with, wherein water spray system is respectively arranged with above three sections of packing layers below, above every section of packing layer
Tower wall on be both provided with inspection chamber；It is configured with what is matched with the pump to connect on hot reuse water pipe in the liquid storage cavity
Liquid storage cylinder body fluid level controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611237561.9A CN106512881B (en) | 2016-12-28 | 2016-12-28 | One kind is used for oxidation barrel steam recovery tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611237561.9A CN106512881B (en) | 2016-12-28 | 2016-12-28 | One kind is used for oxidation barrel steam recovery tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106512881A CN106512881A (en) | 2017-03-22 |
| CN106512881B true CN106512881B (en) | 2018-04-20 |
Family
ID=58338196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611237561.9A Active CN106512881B (en) | 2016-12-28 | 2016-12-28 | One kind is used for oxidation barrel steam recovery tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106512881B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203518661U (en) * | 2013-07-01 | 2014-04-02 | 四川蓝光伟业高新技术有限公司 | Air tower spray condenser with non-filler cooling tower system |
| CN203687681U (en) * | 2013-12-30 | 2014-07-02 | 中空能源设备有限公司 | Energy-saving type air cooling tower |
| CN104645789A (en) * | 2015-02-02 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Multistage circulating washing absorption tower combination equipment |
| CN206372806U (en) * | 2016-12-28 | 2017-08-04 | 浙江华源颜料股份有限公司 | For oxidation barrel steam recovery tower |
-
2016
- 2016-12-28 CN CN201611237561.9A patent/CN106512881B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203518661U (en) * | 2013-07-01 | 2014-04-02 | 四川蓝光伟业高新技术有限公司 | Air tower spray condenser with non-filler cooling tower system |
| CN203687681U (en) * | 2013-12-30 | 2014-07-02 | 中空能源设备有限公司 | Energy-saving type air cooling tower |
| CN104645789A (en) * | 2015-02-02 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Multistage circulating washing absorption tower combination equipment |
| CN206372806U (en) * | 2016-12-28 | 2017-08-04 | 浙江华源颜料股份有限公司 | For oxidation barrel steam recovery tower |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106512881A (en) | 2017-03-22 |
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