CN114288814A - Fixed bed process desulfurizing tower capable of heating and dehumidifying - Google Patents
Fixed bed process desulfurizing tower capable of heating and dehumidifying Download PDFInfo
- Publication number
- CN114288814A CN114288814A CN202111601803.9A CN202111601803A CN114288814A CN 114288814 A CN114288814 A CN 114288814A CN 202111601803 A CN202111601803 A CN 202111601803A CN 114288814 A CN114288814 A CN 114288814A
- Authority
- CN
- China
- Prior art keywords
- air
- heating
- pipe
- fixed bed
- bed process
- 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
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The invention discloses a fixed bed process desulfurizing tower capable of heating and dehumidifying, belonging to the technical field of fixed bed process desulfurization, and comprising a desulfurizing tower body, wherein the bottom of the desulfurizing tower body is provided with a discharging conical section, and the outer wall of the discharging conical section is sleeved with a heating pipeline; the heating pipeline comprises a plurality of layers of air pipes, each layer of air pipe is arranged in an annular shape, adjacent air pipes are communicated through air connecting pipelines, the air inlet end and the air outlet end of each layer of air pipe are arranged oppositely, and air flow of each layer of air pipe is divided into two paths by the air inlet end and then converged by the air outlet end.
Description
Technical Field
The invention relates to the technical field of fixed bed process desulfurization, in particular to a fixed bed process desulfurizing tower capable of heating and dehumidifying.
Background
The statements herein merely provide background information related to the present disclosure and may not necessarily constitute prior art.
At present, the desulfurizer used in the fixed bed process desulfurizing tower is mostly solid and large-particle-shaped, and generally cannot be provided with a heating system, so that the desulfurizing tower can play a better desulfurizing effect and reduce the land area, and measures for reducing the diameter of an absorption tower and increasing the height of the absorption tower can be generally used. After the height of the absorption tower is increased, a large amount of desulfurizer powder is generated due to crushing and breaking when the desulfurizer is charged, and the desulfurizer powder is accumulated on the discharging conical section at the bottom of the absorption tower. The powder is very easy to be wetted and hardened, the discharge opening at the bottom of the absorption tower can be blocked greatly along with the increase of the operation time of the absorption tower, the replacement efficiency of the desulfurizer is reduced, and the desulfurization performance of the whole absorption tower on flue gas is influenced. Therefore, when the fixed bed dry process desulfurization tower reaches a certain height, a heating system is required to be arranged at the bottom.
The current flue gas desulfurization denitration dust removal field has two kinds of forms of electrical heating and steam pipeline heating, and steam pipeline heating is widely used because of low cost, wide application range, high security. Steam heating pipe is mostly S type coil pipe, and each heating surface has two pipeline interface air inlets and gas outlet at least, and the air inlet is in the top of gas outlet, if the heating surface will arrange a plurality of S type coil pipes on a face greatly, the interface of every will have N2, fixes every coil pipe on the heating surface earlier during the installation, connects into again and gives vent to anger female pipe.
The inventor finds that in a fixed bed process desulfurization tower, the space around a bottom discharge conical section is very limited, and the number of S-shaped coil joints is large, so that the operation space is small, the field construction is complicated, the heating is not uniform due to uneven steam distribution caused by the large number of joints, the working state of a heating pipe cannot be monitored in time, and the steam supply cannot be adjusted in real time according to the actual working state.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide a fixed bed process desulfurizing tower capable of heating and dehumidifying, wherein heating pipelines are annularly arranged in a layered manner, the air inlet end and the air outlet end of each layer of air pipe are oppositely arranged, steam is equally divided into two paths to heat half of wall plates simultaneously, the conical hopper can be heated more uniformly, the number of interfaces can be reduced to the maximum extent, the welding workload during installation is reduced, the arrangement of components such as a remote control valve, a temperature sensor and the like can accurately monitor the data such as the flow rate, the usage and the temperature of the steam, meanwhile, the working state of a heating pipe is adjusted in real time based on big data analysis, and the problems that the heating pipe of the existing fixed bed process desulfurizing tower is complicated in arrangement, uneven in heating and incapable of adjusting the working state of the heating pipe in real time are solved.
In order to achieve the purpose, the invention is realized by the following technical scheme:
in a first aspect, the invention provides a fixed bed process desulfurization tower capable of heating and dehumidifying, which comprises a desulfurization tower body, wherein the bottom of the desulfurization tower body is provided with a discharging conical section, and the outer wall of the discharging conical section is sleeved with a heating pipeline; the heating pipeline comprises a plurality of layers of air pipes, each layer of air pipe is arranged in an annular shape, adjacent air pipes are communicated through air connecting pipelines, the air inlet end and the air outlet end of each layer of air pipe are arranged oppositely, and air flow of each layer of air pipe is divided into two paths by the air inlet end and then converged by the air outlet end.
As a further technical scheme, a plurality of layers of air pipes are sequentially arranged on the outer wall of the unloading conical section at intervals from top to bottom.
As a further technical scheme, the air outlet end of the upper-layer air pipe is communicated with the air inlet end of the adjacent lower-layer air pipe through the air receiving pipeline.
As a further technical scheme, the air inlet end of the uppermost layer air pipe is communicated with an air inlet main pipe, the air inlet main pipe is provided with a remote control valve, a first flowmeter, a pressure gauge and a first thermometer, and the remote control valve, the first flowmeter, the pressure gauge and the first thermometer are all connected with a background control system.
As a further technical scheme, the air outlet end of the lowest layer of air pipe is communicated with an air outlet main pipe, the air outlet main pipe is provided with a second flowmeter and a second thermometer, and the second flowmeter and the second thermometer are both connected with a background control system.
As a further technical scheme, the discharging conical section of the desulfurizing tower is also provided with a hygrometer, and the hygrometer is connected with the background control system.
As a further technical scheme, the hygrometer is arranged on the discharge conical section between the upper air pipe and the lower air pipe.
As a further technical scheme, the sizes of the multiple layers of air pipes are reduced from top to bottom in sequence.
As a further technical scheme, the gas receiving pipeline is obliquely arranged along the outer wall of the discharging conical section of the desulfurizing tower.
As a further technical scheme, the adjacent air pipes are arranged in the vertical direction at equal intervals, and the air pipes are rectangular.
The beneficial effects of the invention are as follows:
(1) according to the invention, the heating pipeline is arranged in an annular layered mode, and the air inlet end and the air outlet end are oppositely arranged, so that steam is equally divided into two paths to heat half of the wall plate simultaneously, the conical hopper can be heated more uniformly, the number of interfaces can be reduced to the maximum extent, and the welding workload during installation is reduced.
(2) The heating pipeline is integrally sleeved on the discharging conical section in an assembly mode, compared with an installation mode of an S-shaped heating pipe, the construction speed is greatly improved, and the heating pipeline with the air inlet end and the air outlet end which are symmetrically arranged only needs to be connected with two pipelines, so that the space occupied by the pipelines is reduced.
(3) The steam flow rate, the steam consumption and the steam temperature can be compared, judged and regulated according to the monitored steam values and the preset values in the background control system, and the regulation and control are carried out based on data analysis, so that the safety, the economy and the high efficiency of the regulation and control scheme are ensured.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of this specification, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate exemplary embodiments of the invention and together with the description serve to explain the invention and not to limit the invention.
FIG. 1 is a schematic front view configuration of a heatable desiccant fixed bed process desulfurization tower in accordance with one or more embodiments of the present invention;
FIG. 2 is a schematic bottom view of a heating conduit arrangement in a discharge cone according to one or more embodiments of the present invention;
in the figure: the mutual spacing or size is exaggerated to show the position of each part, and the schematic diagram is only used for illustration;
wherein, 1, a remote control valve; 2. a first flow meter; 3. a pressure gauge; 4. a first thermometer; 5. a hygrometer; 6. a second flow meter; 7. a second thermometer; 8. a desulfurizing tower; 9. a discharge cone section; 10. an air tube; 11. a gas receiving pipeline; 12. a main air inlet pipe; 13. and an air outlet main pipe.
Detailed Description
It is to be understood that the following detailed description is exemplary and is intended to provide further explanation of the invention as claimed. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.
As introduced in the background art, in the existing fixed bed process desulfurization tower, the space around the bottom discharge conical section is very limited, and the number of interfaces of the S-shaped coil is large, so that the operation space is small, the field construction is complicated, the heating is not uniform due to uneven steam distribution caused by the large number of interfaces, the working state of the heating pipe cannot be monitored in time, and the steam supply cannot be adjusted in real time according to the actual working state.
Example 1
In a typical embodiment of the present invention, as shown in fig. 1-2, a fixed bed process desulfurization tower capable of heating and dehumidifying is provided, which comprises a desulfurization tower 8 and a heating pipeline annularly and hierarchically arranged at a discharge conical section 9 of the desulfurization tower.
The desulfurizing tower 8 is a fixed bed process desulfurizing tower, the bottom of the desulfurizing tower is a discharging conical section 9, the discharging conical section is in a conical form with a downward pointed end on the whole, and the heating pipeline is sleeved on the outer wall of the discharging conical section 9 and is arranged in layers.
Specifically, the heating pipeline comprises a plurality of layers of air pipes 10, each layer of air pipe 10 is annularly arranged on the outer wall of the discharging conical section of the desulfurization tower, the plurality of layers of air pipes are arranged at different heights of the outer wall of the discharging conical section one by one, and the sizes of the plurality of layers of air pipes are sequentially reduced from top to bottom; the adjacent air pipes 10 are communicated through an air receiving pipeline 11, so that an integral air flow passage is formed, and the outer wall of the discharging conical section of the desulfurizing tower is heated.
In the implementation, 4 layers of air pipes are arranged, the 4 layers of air pipes are sequentially arranged on the outer wall of the discharging conical section of the desulfurizing tower at intervals from top to bottom, and the sizes of the 4 layers of air pipes are sequentially reduced from top to bottom; each air pipe is annular and is positioned on the height of one cross section of the discharging conical section of the desulfurizing tower, the adjacent air pipes are communicated by an air connecting pipe, the air connecting pipe is obliquely arranged along the outer wall of the discharging conical section of the desulfurizing tower, the air connecting pipes connected with the same air pipe are oppositely arranged on two sides of the air connecting pipe, namely, the air connecting pipe connected with one air pipe and the upper air pipe is positioned on one side of the air pipe, and the air connecting pipe connected with the lower air pipe is positioned on the other side of the air pipe; the vertical spacing between adjacent air tubes may be set equidistant.
The strengthening rib is avoided to the tracheal inlet end of each layer and the end of giving vent to anger, and the tracheal inlet end of each layer and the end of giving vent to anger symmetry as far as possible place, and the tracheal inlet end of giving vent to anger of upper strata communicates through connecing the trachea way rather than the tracheal inlet end of the next adjacent layer, and the tracheal inlet end of the superiors communicates with female pipe 12 that admits air, and the tracheal end of giving vent to anger of the lowest floor communicates with female pipe 13 that gives vent to anger. That is, the air connecting pipes 11 connecting the adjacent air pipes are symmetrically arranged at intervals.
Such setting is when steam enters from the tracheal inlet end of the superiors, two the tunnel is equallyd divide to steam, heat half wallboard simultaneously, merge a department and get into the next floor afterwards, every gets into one deck trachea, all by the inlet end converge then divide into two tunnel by the inlet end and converge by the end of giving vent to anger and get into the next floor, so circulate, finally the end of giving vent to anger of the lower floor merges a department and discharges into the female pipe of gas and make its heating even, the steam volume of importing and exporting is the same, so heating temperature can carry out more accurate control, in order to reach the purpose of practicing thrift the cost.
In this scheme, every layer sets up the form of round annular trachea, and heating pipeline only needs two pipelines, and the welding work volume of saving the job site that not only can be furthest has still reduced interface quantity, has vacated other equipment of space installation as big as possible for the desulfurizing tower bottom.
In order to be more convenient for the installation of the heating pipeline, the trachea on each layer is firstly assembled and welded, then the whole assembly of the heating pipeline on the discharging conical section is carried out, so that the whole set of heating pipeline is directly sleeved on the discharging conical section, then, the trachea on each layer is spot-welded on the conical hopper wall plate to realize fixation, and the installation of the heating pipeline is more quickly and conveniently realized by the installation mode of the assembly type.
It can be understood that the optimal arrangement scheme of the air inlet end and the air outlet end of the air pipe is symmetrical, so that the steam entering from the air inlet end can be equally divided into two paths, and half of the wall plates are heated at the same time, but the specific arrangement position is determined according to the position of the actual discharge conical section reinforcing rib, as long as the air inlet end and the air outlet end of each layer of heating coil pipe can be arranged symmetrically as far as possible, and the arrangement scheme is not limited too much.
In this embodiment, because the transversal rectangle of personally submitting of desulfurizing tower conical segment of unloading, so also set up tracheal shape into the rectangle, tracheal size is according to the outer wall size setting of the conical segment of unloading of position, makes the laminating setting that the trachea can be better at the conical segment outer wall of unloading, can guarantee the heating effect of the conical segment of unloading. The size of the uppermost trachea is the largest and the size of the lowermost trachea is the smallest.
In order to be able to control the operation of the heating coil accurately, the present embodiment is further provided with a remote control valve 1, a thermometer, a hygrometer, a flow meter, and other measuring elements.
Specifically, the air inlet end of the uppermost layer of air pipe is communicated with an air inlet main pipe 12, a remote control valve 1, a first flowmeter 2, a pressure gauge 3 and a first thermometer 4 are arranged on the air inlet main pipe 12, and the remote control valve 1, the first flowmeter 2, the pressure gauge 3 and the first thermometer 4 are all connected with a background control system and are mainly used for monitoring the temperature, the pressure and the flow of steam at the air inlet end of the heating pipeline and performing regulation and control;
the air outlet end of the lowest air pipe is communicated with an air outlet main pipe 13, a second flowmeter 6 and a second thermometer 7 are arranged on the air outlet main pipe, and the second flowmeter 6 and the second thermometer 7 are also connected with a background control system.
The thermometer is mainly used for checking the integral heating condition of the conical section, comparing the integral heating condition with the desulfurizing agent humidity and the heating time, and obtaining a corresponding numerical relation for data analysis.
The discharging conical section of the desulfurizing tower is also provided with a hygrometer 5, the selectable setting position of the hygrometer is the discharging conical section between the upper and lower adjacent air pipes, and the humidity value of the desulfurizing agent is detected; the hygrometer 5 is connected with the background control system, and the hygrometer is mainly used for measuring the humidity of the desulfurizer in the discharging conical section and transmitting the measured humidity value of the desulfurizer to the background control system, and the background control system determines the adjustment scheme according to the received humidity value of the desulfurizer and parameters such as the temperature and the flow of steam.
The concrete form and the position of setting up of hygrometer do not do the restriction, realize monitoring the humidity of desulfurizer can, if the appearance must be in the leakproofness that the conical section trompil then need to pay attention to each position connection, prevent that the flue gas from revealing.
The background control system is preset with an optimal humidity value and a parameter range of normal work of each instrument, and mainly has the functions of regularly summarizing data returned by the instruments, analyzing according to the data, adjusting the optimal humidity, further analyzing the relation among steam consumption, temperature, desulfurizer humidity, weather and cost, adjusting to the most energy-saving, safest and most economical parameter scheme, and simultaneously monitoring the working states of the heating coil and each instrument.
The specific regulating and controlling thought is as follows: the heating temperature of the discharging conical section is regulated and controlled by controlling the steam flow, and the steam flow is assisted to be controlled by instrument feedback data (flow, force and humidity).
The humidity value of the desulfurizer agglomeration is determined through experiments, the optimal humidity value which is economic and suitable is input into a background control system, a hygrometer 5 monitors the humidity value of the desulfurizer in the discharging conical section and transmits a measured value to the background control system for comparison, the background control system controls a remote control valve 1 to act by taking the measured value as a judgment value, so that the steam flow is controlled, the temperatures of the desulfurizer in the discharging conical section and the discharging conical section are controlled, and the background control system can select full-automatic control or manual control.
Specifically, the background control system receives a monitoring value transmitted by the hygrometer 5, and when the monitoring value is in a set optimal humidity value range, the background control system judges that the heating pipeline at the discharging conical section is in a normal state, the remote control valve 1 does not act at the moment, the steam flow is constant, and the temperature of the desulfurizer in the discharging conical section is constant.
When the background control system receives a monitoring value transmitted by the hygrometer 5 and the monitoring value is lower than a set optimal humidity value range, the humidity of a desulfurizer in the discharging conical section is too low, namely the temperature in the discharging conical section is too high, cooling control is needed, and the reduction of steam consumption is taken as a main regulation measure;
the background control system judges that the heating coil at the discharging conical section is in a high-temperature state, the background control system gives a control instruction of cooling regulation, the remote control valve 1 automatically acts after receiving the command, the valve is gradually closed, the steam flow is reduced, the temperature of the desulfurizer in the discharging conical section is reduced, and the regulation is finished until the humidity value of the desulfurizer returns to the optimal numerical range.
In other embodiments, the valve can be controlled manually, that is, after the background control system gives a control instruction of "cooling control", the remote control valve 1 is controlled manually to close the valve gradually, so that the steam flow is reduced, the temperature of the desulfurizer in the discharge conical section is reduced until the humidity value of the desulfurizer returns to the optimal value range, the control is finished, that is, the control of the valve can be controlled automatically or manually, and the specific control mode can be selected automatically, so that excessive limitation is not imposed.
When the background control system receives a monitoring value transmitted by the hygrometer 5 and the monitoring value is higher than a set optimal humidity value range, the humidity of the desulfurizer in the discharging conical section is too high, namely the temperature in the discharging conical section is too low, temperature rise control is needed, and at the moment, the increase of steam consumption is taken as a main regulation and control measure to prevent the desulfurizer from being hardened due to the continuous increase of the humidity;
the background control system judges that the heating coil at the discharging conical section is in a low-temperature state, the background control system gives a control instruction of heating regulation, the remote control valve 1 automatically acts after receiving the instruction, the valve is gradually opened, the steam flow is increased, the temperature of the desulfurizer in the discharging conical section is further increased until the humidity value of the desulfurizer returns to the optimal numerical range, and the regulation is finished.
In the process of controlling the action of the remote control valve 1 through the background control system, the opening of the remote control valve 1 is monitored through the background control system, when the valve reaches the limit position of the valve, the valve stops acting, and the background control system gives an alarm.
Similarly, in other embodiments, the valve may be manually controlled, that is, after the background control system gives a control instruction of "temperature rise control", the remote control valve 1 is manually controlled to gradually open the valve, so that the steam flow is increased, and the temperature of the desulfurizing agent in the discharging conical section is increased until the humidity value of the desulfurizing agent returns to the optimal value range, and the control is finished, that is, the control of the valve may be automatically controlled or manually controlled, and the specific control mode may be automatically selected, which does not impose too much restriction.
The background control system can not only regulate and control the work of the heating coil, but also monitor the working state of the heating pipeline in the regulating and controlling process and send out abnormal warning.
For convenience of understanding, the present embodiment is described by taking four abnormal states, i.e., blockage, air leakage, high pressure abnormality, and instrument and valve abnormality, as follows:
1. blocking;
the blockage is divided into two cases, one is the blockage of the main pipe, and the other is the blockage of the heating pipeline.
Blocking a main pipe: the background control system receives monitoring values of all monitoring instruments, when the numerical values of a first flowmeter 2 at the air inlet main pipe and a second flowmeter 6 at the air outlet main pipe are 0 or tend to 0, the numerical values of a first thermometer 4 at the air inlet main pipe and a second thermometer 7 at the air outlet main pipe are reduced at the same time, and the numerical value change of all monitoring instruments cannot be influenced or the influence is small by the action of the remote control valve 1, the main pipe is judged to be blocked.
The main pipe blockage is divided into two conditions of air inlet main pipe blockage and air outlet main pipe blockage, at the moment, the pressure gauge 3 is combined for further judgment, when the numerical value of the pressure gauge 3 has pressure and the pressure is basically unchanged, the air outlet main pipe blockage is formed, the background control system sends a judgment instruction of 'air outlet main pipe blockage', simultaneously closes the remote control valve 1, and sends an abnormal warning;
when the numerical value of the pressure gauge 3 has no pressure or the pressure tends to 0, the air inlet main pipe is blocked, the background control system sends a judgment instruction of 'the air inlet main pipe is blocked', and simultaneously, the remote control valve 1 is closed and an abnormal warning is sent.
And (3) blocking of the heating coil: the background control system receives the monitoring values of each monitoring instrument, when the first flowmeter 2 at the air inlet main pipe and the second flowmeter 6 at the air outlet main pipe are 0 or tend to 0, the first thermometer 4 at the air inlet main pipe and the second thermometer 7 at the air outlet main pipe are reduced, the temperature reduction speed at the air outlet main pipe is higher than that of the air inlet main pipe, the numerical value change of each monitoring instrument cannot be influenced by the action of the remote control valve 1, or the influence is small, the main pipe is judged to be blocked, at the moment, the background control system sends a judgment instruction of 'heating coil blockage', the remote control valve 1 is closed at the same time, and an abnormal warning is sent.
2. Air leakage;
in the present embodiment, the heating duct leakage is taken as an example for explanation.
Specifically, the background control system receives monitoring values of the flowmeters, the first flowmeter 2 at the air inlet main pipe is larger than the second flowmeter 6 at the air outlet main pipe, the difference value of the flow rates of the air inlet main pipe and the air outlet main pipe tends to a certain value when the remote control valve 1 acts, the value is larger than an allowable difference value, at the moment, the background control system sends a judgment instruction of heating pipeline air leakage, simultaneously closes the remote control valve 1, and sends an abnormal warning.
3. High pressure anomaly;
the high pressure is unusual mainly monitors the pressure of steam in the female pipe of admitting air, and then judges the abnormal degree of heating pipe internal pressure, and is specific, utilizes manometer 3 on the female pipe of admitting air to monitor the pressure of steam in the female pipe of admitting air to transmit monitoring value to backstage control system, when this monitoring value surpassed the high pressure safety value of preset, backstage control system judged "high pressure unusual", control remote control valve 1 and close, sent unusual warning simultaneously.
4. Instrument, valve anomaly;
the background control system automatically establishes a data model for data fed back by various instruments and valves, compares the data with historical data at regular time, judges that the instruments and the valves are abnormal if a certain data is abnormal, sends an abnormal warning to inquire whether the valves are turned off, and automatically turns off the remote control valves 1 by default if no operation is performed within a period of time.
It is understood that in other embodiments, the flow meter, the pressure gauge, the thermometer, the flow meter, and the like may be replaced by sensors, as long as monitoring and transmission of monitoring data are possible, which is not limited herein.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. A fixed bed process desulfurizing tower capable of heating and dehumidifying is characterized by comprising a desulfurizing tower body, wherein the bottom of the desulfurizing tower body is provided with a discharging conical section, and the outer wall of the discharging conical section is sleeved with a heating pipeline; the heating pipeline comprises a plurality of layers of air pipes, each layer of air pipe is arranged in an annular shape, adjacent air pipes are communicated through air connecting pipelines, the air inlet end and the air outlet end of each layer of air pipe are arranged oppositely, and air flow of each layer of air pipe is divided into two paths by the air inlet end and then converged by the air outlet end.
2. The fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 1, wherein a plurality of air pipes are arranged at intervals on the outer wall of the discharge cone section from top to bottom in sequence.
3. The fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 2, wherein the gas outlet end of the upper layer gas pipe is communicated with the gas inlet end of the adjacent lower layer gas pipe through the gas connecting pipe.
4. The fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 1, wherein the inlet end of the uppermost gas pipe is communicated with a gas inlet main pipe, the gas inlet main pipe is provided with a remote control valve, a first flowmeter, a pressure gauge and a first thermometer, and the remote control valve, the first flowmeter, the pressure gauge and the first thermometer are all connected with the background control system.
5. The fixed bed process desulfurizing tower capable of being heated and dehumidified as claimed in claim 1, wherein the gas outlet end of the lowest layer gas pipe is communicated with a gas outlet main pipe, the gas outlet main pipe is provided with a second flowmeter and a second thermometer, and the second flowmeter and the second thermometer are both connected with a background control system.
6. The fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 1, wherein the discharging cone section of the desulfurization tower is further provided with a hygrometer, and the hygrometer is connected with a background control system.
7. A heatable dehumidification fixed bed process desulfurization tower as in claim 6 wherein said hygrometer is located at the discharge cone between the upper and lower adjacent gas tubes.
8. The fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 1, wherein the size of the multi-layered air pipes is decreased from the top to the bottom in sequence.
9. A fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 1, wherein said gas piping is disposed obliquely along an outer wall of a discharge cone section of the desulfurization tower.
10. A fixed bed process desulfurization tower capable of heating and dehumidifying as claimed in claim 1, wherein adjacent gas pipes are arranged at equal intervals in the vertical direction, and the gas pipes have a rectangular shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111601803.9A CN114288814B (en) | 2021-12-24 | 2021-12-24 | Fixed bed process desulfurizing tower capable of heating and dehumidifying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111601803.9A CN114288814B (en) | 2021-12-24 | 2021-12-24 | Fixed bed process desulfurizing tower capable of heating and dehumidifying |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114288814A true CN114288814A (en) | 2022-04-08 |
| CN114288814B CN114288814B (en) | 2022-09-16 |
Family
ID=80968954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202111601803.9A Active CN114288814B (en) | 2021-12-24 | 2021-12-24 | Fixed bed process desulfurizing tower capable of heating and dehumidifying |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114288814B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB695812A (en) * | 1949-10-17 | 1953-08-19 | Fmc Corp | Improvements in or relating to methods and apparatus for the recovery of condensableconstituents from hot gaseous mixtures |
| CN102168928A (en) * | 2011-03-09 | 2011-08-31 | 娄底市兴华有色金属有限公司 | Butt clamp heat exchanger for preheating air by using waste heat of flue gas |
| CN103043925A (en) * | 2012-12-21 | 2013-04-17 | 张克海 | Lime kiln with heat energy recovery system |
| CN204063847U (en) * | 2014-08-12 | 2014-12-31 | 北京电力设备总厂 | A kind of system and device of Low Temperature Steam contact drying brown coal |
| CN209820065U (en) * | 2019-01-24 | 2019-12-20 | 山东汇润膳食堂股份有限公司 | Konjaku flour drying device |
| CN210802134U (en) * | 2019-06-06 | 2020-06-19 | 湖北江田精密化学有限公司 | Built-in coil pipe type liquid heat exchange device |
| CN212262886U (en) * | 2020-04-30 | 2021-01-01 | 山东国舜建设集团有限公司 | Quick cleaning device behind CFB semi-dry process desulfurizer bed collapse |
| CN112807985A (en) * | 2021-02-03 | 2021-05-18 | 陕西龙门钢铁有限责任公司 | Device for accelerating ash discharge of desulfurization dust removal ash bin |
-
2021
- 2021-12-24 CN CN202111601803.9A patent/CN114288814B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB695812A (en) * | 1949-10-17 | 1953-08-19 | Fmc Corp | Improvements in or relating to methods and apparatus for the recovery of condensableconstituents from hot gaseous mixtures |
| CN102168928A (en) * | 2011-03-09 | 2011-08-31 | 娄底市兴华有色金属有限公司 | Butt clamp heat exchanger for preheating air by using waste heat of flue gas |
| CN103043925A (en) * | 2012-12-21 | 2013-04-17 | 张克海 | Lime kiln with heat energy recovery system |
| CN204063847U (en) * | 2014-08-12 | 2014-12-31 | 北京电力设备总厂 | A kind of system and device of Low Temperature Steam contact drying brown coal |
| CN209820065U (en) * | 2019-01-24 | 2019-12-20 | 山东汇润膳食堂股份有限公司 | Konjaku flour drying device |
| CN210802134U (en) * | 2019-06-06 | 2020-06-19 | 湖北江田精密化学有限公司 | Built-in coil pipe type liquid heat exchange device |
| CN212262886U (en) * | 2020-04-30 | 2021-01-01 | 山东国舜建设集团有限公司 | Quick cleaning device behind CFB semi-dry process desulfurizer bed collapse |
| CN112807985A (en) * | 2021-02-03 | 2021-05-18 | 陕西龙门钢铁有限责任公司 | Device for accelerating ash discharge of desulfurization dust removal ash bin |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114288814B (en) | 2022-09-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2023236701A1 (en) | Anti-blocking purging system for acoustic temperature measurement device of coal-fired boiler, and method for using same | |
| CN114288814B (en) | Fixed bed process desulfurizing tower capable of heating and dehumidifying | |
| CN113532787B (en) | Measurement and control device of heat storage heater for wind tunnel experiment | |
| CN205747349U (en) | A kind of air-conditioning monitoring and controlling system | |
| CN215803265U (en) | Bulky concrete temperature alarm device | |
| CN104630403B (en) | The burning stove control method of a kind of top combustion stove and burning furnace control system | |
| CN205329213U (en) | Automatic carminative diphenyl heat preservation system | |
| CN105699023A (en) | Measuring device and method suitable for carbon dioxide pipeline exhaust and leakage test | |
| CN107502694A (en) | A kind of shaft furnace inlet duct and shaft furnace air inlet method | |
| CN109487025B (en) | Furnace top nitrogen system | |
| US20240167708A1 (en) | System and method for controlling temperature and water content of an airstream | |
| CN214635422U (en) | Air preheater anti-blocking treatment device based on denitration ammonia escape control | |
| CN214437707U (en) | Desulfurization island bed pressure drop control system | |
| CN108007217B (en) | Pneumatic conveying system and method for activated carbon by utilizing waste heat | |
| CN212866312U (en) | Bulky concrete temperature control system | |
| KR101605206B1 (en) | Appartus for controlling hot-air temperature in hot stove system | |
| CN212986228U (en) | Air quantity measuring and automatic regulating device | |
| CN212206771U (en) | High-precision constant-current dilution time-sharing synchronous zoning type CO measuring system for flue of coal-fired power plant | |
| CN2901115Y (en) | Air conditioner refrigeration system | |
| CN209519561U (en) | Plateau type oxygenerator | |
| CN208125384U (en) | A kind of engine aspirating system | |
| CN208560956U (en) | A kind of equipment of powder material Dense Phase Pneumatic Conveying | |
| US5709173A (en) | Method and apparatus for controlling combustion air in a boiler plant | |
| US7614613B2 (en) | Method of operating a cooling fluid system | |
| CN214915910U (en) | Distributor system in reactor and reactor |
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 | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A Fixed Bed Desulfurization Tower with Heating and Dehumidification Effective date of registration: 20221228 Granted publication date: 20220916 Pledgee: Qilu bank Limited by Share Ltd. Ji'nan Changqing branch Pledgor: SHANDONG GUOSHUN CONSTRUCTION GROUP Co.,Ltd. Registration number: Y2022980029384 |