CN102901093A - Double-way controllable material returning valve for circulating fluidized bed boiler - Google Patents
Double-way controllable material returning valve for circulating fluidized bed boiler Download PDFInfo
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- CN102901093A CN102901093A CN2012103903345A CN201210390334A CN102901093A CN 102901093 A CN102901093 A CN 102901093A CN 2012103903345 A CN2012103903345 A CN 2012103903345A CN 201210390334 A CN201210390334 A CN 201210390334A CN 102901093 A CN102901093 A CN 102901093A
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Abstract
The invention discloses a double-way controllable material returning valve for a circulating fluidized bed boiler, belongs to a material returning device of a circulating fluidized bed boiler and in particular relates to a flow rate regulating device. According to the double-way controllable material returning valve, a partition plate is arranged in a material charging pipe of the material returning valve, the lower part of the material charging pipe is partitioned into two parts, each of the two parts is connected with a moving filling bed, the moving filling beds are respectively connected with two material returning beds, material returning pipes are connected behind the material returning beds, and air distribution systems are respectively arranged on the lower parts of the moving filling beds and the material returning beds. The material returning valve has two loops, so that materials are charged at a single point and returned at a plurality of points; and according to a flow rate controlling principle of the material returning valve, pressure of the material charging pipe on two sides of the partition plate is changed by regulating the volume of flexible air on the lower parts of the two moving filling beds, so that a material charging ratio in which materials on the upper part of the material charging pipe are charged into two sides of the lower part of the partition plate is regulated, and the material flow rates at two material returning points are regulated. By the material returning valve, the materials can be uniformly charged into a hearth, so that the material returning uniformity of hot materials in cross sections of the beds of the large-scale circulating fluidized bed boiler is greatly increased.
Description
Technical field
The present invention relates to a kind of controllable device of material returning valve of CFBB, belong to the material-returning device of CFBB.
Background technology
Technology of Circulating Fluidized Bed Boiler is a high-efficiency low-pollution clean burning branch art that develops rapidly in recent ten years.This technology has obtained widely commercial the application in fields such as station boiler, Industrial Boiler and offal treatment utilizations in the world, and develops to the large circulating fluidized bed boiler of hundreds of thousands multikilowatt scale; Domestic research, development and application is in this respect also risen gradually, among existing up to a hundred CFBBs put into operation or making.Therefore the raising tool of CFB Boiler Efficiency is of great significance.
Material returning valve is very important parts in the CFBB as the device of loopback of material.The performance of material returning valve directly has influence on the stability of fluid bed outer circulation and the uniformity that the interior material of stove distributes, thereby affects the efficient of fluid bed.The effect of material returning valve mainly is returning charge and sealing function, and namely material is back to burner hearth by material returning valve, prevents that again the flue gas of burner hearth from affecting the efficient of separator from the material returning valve anti-channeling to cyclone separator simultaneously.
The subject matter that present China circulating fluidized bed technique faces is, maximization along with CFBB, the burner hearth bed surface amasss also corresponding increase, owing to the restriction of material horizontal proliferation speed, has occurred the deviation of serious temperature and material concentration cross direction profiles in the boiler operatiopn.Wherein the inhomogeneous adjusting coal supply deviation that can adopt of temperature solves, and is adjusted but the material concentration that is caused by circulation flow-rate deviation between each separator diffusion inequality still lacks enough methods of operating.
Mainly adopt single channel material returning valve device both at home and abroad, namely each material returning valve only has outlet of an import, and this single channel material-returning device returning charge point is few, causes that easily material distributes inequality in the burner hearth, also is not suitable in the large-sized boiler.Harbin Boiler Plant has been invented a kind of pneumatic self-balancing two-way feeding back device (patent No. is ZL 200620020679.1), has realized the single-point charging, and the function of 2 returning charges can be assigned to the outer circulation material larger bed surface long-pending more equably.But in actual motion, this pneumatic self-balancing returning charge valve can't be realized the manual control of recycle stock flow rate between two returning charge points, namely can't according to the artificial returning charge amount of regulating two material points of actual condition, therefore can not solve better the uneven problem of material distribution in the burner hearth.
Summary of the invention
For above-mentioned situation, the invention provides the controlled material returning valve device of a kind of CFBB two-way, when having realized the returning charge of single-point charging multiple spot, can control the flow rate of the material between each returning charge point distributes, thereby optimize the material allocation performance, solve better the problem of material maldistribution in the burner hearth.
Purpose of the present invention and task are achieved through the following technical solutions:
The controlled material returning valve of a kind of two-way of CFBB, this material returning valve comprises feed pipe, air-distribution device, and the moving packed bed, baffling section, returning charge bed and the refeed line that are arranged symmetrically in both sides, feed pipe bottom; Described moving packed bed is connected by the baffling section with the returning charge bed, and link to each other with the air compartment of air-distribution device respectively, it is characterized in that: in feed pipe, be provided with demarcation strip, feed pipe is divided into two parts, the demarcation strip bottom links to each other with air distribution plate, and the demarcation strip top will be higher than 0.2 meter of refeed line air outlet top edge at least.
In the technique scheme, the outer surface of described demarcation strip is provided with the Fire and abrasion resistant material layer.Described baffling section adopts one section horizontal tube or heat-resisting dividing plate.
Another technical characterictic of the present invention also is: two moving packed beds link to each other with a loosening wind air compartment separately, and two returning charge beds link to each other with a returning charge wind air compartment separately.
The present invention has the following advantages and the high-lighting effect: owing to being provided with demarcation strip in the feed pipe hypomere feed pipe hypomere is divided into two parts, link to each other with moving packed bed respectively, by regulating the size of the loosening wind air quantity under two moving packed beds, can change the pressure of demarcation strip both sides feed pipe, the ratio when thereby the material of regulating the feed pipe epimere enters hypomere demarcation strip both sides realizes the adjusting to two returning charge point material flow rates.
Description of drawings
Fig. 1 is the structural representation of a kind of controlled material returning valve of two-way for CFBB provided by the invention.(being top view).
Fig. 2 is the A-A cutaway view of Fig. 1.
Among the figure: the 1-feed pipe; The 2-demarcation strip; The 3-refeed line; 4-baffling section; The 5-air distribution plate; 6-returning charge bed; The 7-moving packed bed;
8-becomes flexible the wind air compartment; 9-returning charge wind air compartment; 10-Fire and abrasion resistant material layer; 11-becomes flexible wind air compartment pressure tap
12-low level pressure tap; 13-high-order pressure tap; 14-refeed line air outlet top edge.
The specific embodiment
Below in conjunction with accompanying drawing structure of the present invention, principle and the specific embodiment are described further.
The controlled material returning valve of this two-way comprises feed pipe, air-distribution device, and the moving packed bed 7, baffling section 4, returning charge bed 6 and the refeed line 3 that are arranged symmetrically in both sides, feed pipe bottom; Described moving packed bed 7 is connected by baffling section 4 with returning charge bed 6, and moving packed bed links to each other with the air compartment of air-distribution device respectively with the returning charge bed; Be provided with demarcation strip in feed pipe 1, feed pipe is divided into two parts, the demarcation strip bottom links to each other with air distribution plate 5.The demarcation strip top will be higher than refeed line air outlet top edge 14, generally will exceed at least 0.2 meter.
The diameter of feed pipe is 1300mm in the present embodiment.The demarcation strip outer surface is lined with Fire and abrasion resistant material (such as phosphoric acid block salt, carbofrax material etc.), and the aspect ratio refeed line air outlet top edge of demarcation strip exceeds 1.5m.
Moving packed bed 7 is connected with the returning charge bed by a baffling section 4 connections, to increase the flowability of returning charge.This baffling section 4 can be one section horizontal tube, also can adopt heat-resisting dividing plate to realize the baffling function.The top edge of baffling section is lower than the lower limb 300mm of refeed line air outlet at least.The recommended levels length of tube is less than 250mm during the usage level pipe, and the suggestion block board thickness is 100mm when using heat-resisting dividing plate.Baffling Duan Weiyi section horizontal tube in the present embodiment, the width of this baffling section is 200mm.Material returning valve refeed line air outlet lower limb is higher than baffling section top edge 350mm.
The air compartment of air-distribution device can be square air compartment, also can adopt tapered air compartment.The loosening wind air compartment 8 and the returning charge wind air compartment 9 that use in the present embodiment all are square air compartments, and area is 750*750mm.
Realize in this example that the controlled concrete grammar of Circulating Fluidized Bed flow rate is as follows: two moving packed beds link to each other with a loosening wind air compartment 8 separately, and two returning charge beds link to each other with a returning charge wind air compartment 9 separately.Use the advantage of independent air compartment to be, by adjusting this returning charge point returning charge wind, the air quantity of loosening wind can be realized the control to this returning charge point Flow of Goods and Materials.
In two loosening wind air compartments, two pressure taps 11 are set, because the constant resisting force of air distribution plate in the device, so in fact the pressure of air compartment pressure tap 11 reflected the controlling level of moving packed bed China and foreign countries circulated material quantities, in moving packed bed, arrange barometric gradient low level measurement point 12 and high-order pressure tap 13, wherein high-order pressure tap 13 and refeed line air outlet upper edge are on the same level line, because high-low-position measuring point difference in height is constant, therefore pass through the measurement of high-low-position pressure, can obtain material pressure gradient in the moving packed bed by conversion, theoretical according to viscous glide stream, the material differential pressure gradients has directly been reacted the size of material flow rate.By changing the loosening wind air quantity of certain side shifting packed bed, height and the barometric gradient of sealing leg material level will change in the corresponding feed pipe, and then the material of regulating the feed pipe epimere ratio that enters hypomere demarcation strip both sides, realize the adjusting to two returning charge point material flow rates.
Claims (4)
1. controlled material returning valve of two-way that is used for CFBB, this material returning valve comprises feed pipe (1), air-distribution device, and the moving packed bed (7), baffling section (4), returning charge bed (6) and the refeed line (3) that are arranged symmetrically in both sides, feed pipe bottom; Described moving packed bed (7) is connected by baffling section (4) with returning charge bed (6), and links to each other with the air compartment of air-distribution device respectively, it is characterized in that: be provided with demarcation strip (2) in feed pipe, feed pipe is divided into two parts; The demarcation strip bottom links to each other with air distribution plate (5), and the demarcation strip top will be higher than (14) 0.2 meters of refeed line air outlet top edges at least.
2. the controlled material returning valve of a kind of two-way for CFBB as claimed in claim 1, it is characterized in that: the outer surface of described demarcation strip is provided with Fire and abrasion resistant material layer (10).
3. the controlled material returning valve of a kind of two-way for CFBB as claimed in claim 1 is characterized in that: described baffling section one section horizontal tube of employing or heat-resisting dividing plate.
4. the controlled material returning valve of a kind of two-way for CFBB as claimed in claim 1, it is characterized in that: two moving packed beds link to each other with a loosening wind air compartment (8) separately, and two returning charge beds link to each other with a returning charge wind air compartment (9) separately.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104696951A (en) * | 2015-01-28 | 2015-06-10 | 中国神华能源股份有限公司 | Boiler-in integrated coupled desulfurization and denitrification method for circulating fluidized bed boiler |
CN104930502A (en) * | 2015-05-14 | 2015-09-23 | 中国矿业大学 | Multichannel distributing device suitable for multi-bed system circulating material balance control |
WO2020039117A1 (en) | 2018-08-24 | 2020-02-27 | Sumitomo SHI FW Energia Oy | An arrangement for and a method of controlling flow of solid particles and a fluidized bed reactor |
CN115585455A (en) * | 2022-12-12 | 2023-01-10 | 浙江百能科技有限公司 | Furnace body system based on bidirectional material returning device and control method thereof |
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CN1932378A (en) * | 2005-09-13 | 2007-03-21 | 中国科学院工程热物理研究所 | Circulating fluid bed ash pneumatic control distributing valve |
CN200989582Y (en) * | 2006-04-26 | 2007-12-12 | 哈尔滨锅炉厂有限责任公司 | Pneumatic automatic balancing double-way return material valve used for fluidized bed boiler |
CN201954536U (en) * | 2011-01-27 | 2011-08-31 | 华西能源工业股份有限公司 | Return device of large-scale circulating fluidized bed |
CN202884910U (en) * | 2012-10-15 | 2013-04-17 | 清华大学 | Double-loop controllable material returning valve used for circulating fluidized bed boiler |
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2012
- 2012-10-15 CN CN2012103903345A patent/CN102901093A/en active Pending
Patent Citations (5)
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JPS59142304A (en) * | 1983-02-03 | 1984-08-15 | Mitsubishi Heavy Ind Ltd | Fluidized-bed combustion furnance |
CN1932378A (en) * | 2005-09-13 | 2007-03-21 | 中国科学院工程热物理研究所 | Circulating fluid bed ash pneumatic control distributing valve |
CN200989582Y (en) * | 2006-04-26 | 2007-12-12 | 哈尔滨锅炉厂有限责任公司 | Pneumatic automatic balancing double-way return material valve used for fluidized bed boiler |
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CN202884910U (en) * | 2012-10-15 | 2013-04-17 | 清华大学 | Double-loop controllable material returning valve used for circulating fluidized bed boiler |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104696951A (en) * | 2015-01-28 | 2015-06-10 | 中国神华能源股份有限公司 | Boiler-in integrated coupled desulfurization and denitrification method for circulating fluidized bed boiler |
CN104930502A (en) * | 2015-05-14 | 2015-09-23 | 中国矿业大学 | Multichannel distributing device suitable for multi-bed system circulating material balance control |
WO2020039117A1 (en) | 2018-08-24 | 2020-02-27 | Sumitomo SHI FW Energia Oy | An arrangement for and a method of controlling flow of solid particles and a fluidized bed reactor |
KR20210046040A (en) * | 2018-08-24 | 2021-04-27 | 스미토모 에스에이치아이 에프더블유 에너지아 오와이 | Solid particle flow control device and method and fluidized bed reactor |
CN112867559A (en) * | 2018-08-24 | 2021-05-28 | 住友重机械福惠能源有限公司 | Arrangement for controlling a flow of solid particles, method thereof and fluidized bed reactor |
US11331637B2 (en) | 2018-08-24 | 2022-05-17 | Sumitomo SHI FW Energia Oy | Arrangement for and a method of controlling flow of solid particles and a fluidized bed reactor |
KR102539819B1 (en) * | 2018-08-24 | 2023-06-02 | 스미토모 에스에이치아이 에프더블유 에너지아 오와이 | Apparatus and method for controlling flow of solid particles and fluidized bed reactor |
CN115585455A (en) * | 2022-12-12 | 2023-01-10 | 浙江百能科技有限公司 | Furnace body system based on bidirectional material returning device and control method thereof |
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Application publication date: 20130130 |