fluidized combustion 中文意思是什麼

fluidized combustion 解釋
流化床焚燒
  • fluidized : 流化的
  • combustion : n. 1. 燃燒,發火,點火。2. (有機體內營養料的)氧化。3. 騷動。
  1. Afbc atmospheric fluidized bed combustion

    大氣流化床燃燒
  2. Bed temperature and mainstream pressure are important parameter of circulating fluidized bed boiler ( cfbb ) combustion control system. to maintain them normal is key to the stable and economic operation of cfbb

    床溫和主汽壓是循環流化床鍋爐燃燒控制系統中的兩個重要參數,維持正常的床溫和主汽壓是循環流化床鍋爐穩定、經濟運行的關鍵。
  3. Analyses of rheological properties of coal - water mixture for pressurized fluidized bed combustion

    增壓流化床煤水混合物流變特性影響因素分析
  4. Experimental study on fluidized bed agglomeration combustion using fly - ash slurry with high carbon content and coal - water mixture as fuels

    高含碳飛灰泥與煤水混合物流化床結團燃燒試驗研究
  5. Application and development of washary tailings fluidized bed combustion technology

    洗煤泥沸騰燃燒技術的應用與發展
  6. Design and combustion technology of density msw fluidized bed incinerator

    流化床垃圾焚燒爐設計和焚燒工藝的研究
  7. In this case, circulating fluidized bed boiler has become the first new technology of high efficiency and low pollution. this paper simply introduce the clean combustion of circulating fluidized bed boiler and explore the sulfur capture, nitrogen capture, dust capture, slag excluding and using by connecting with the practically case of bt - 75 / 4. 2 - m circulating fluidized bed boiler in yth group

    本文對循環流化床鍋爐的潔凈燃燒在理論上做了簡要的論述,並結合雲天化股份公司的bt - 75 4 . 2 - m型循環流化床鍋爐的實際運行情況,對循環流化床鍋爐燃燒過程中的脫硫、脫氮,煙氣的除塵、灰渣的排放和利用等情況進行了探討。
  8. Coal - char pyrolysis, firing, burnt and limestone calcination under o _ ( 2 ) / n _ ( 2 ) oro _ ( 2 ) / co _ ( 2 ) atmosphere were carried on a thermobalance. limestone calcination and sulfuration under o _ ( 2 ) / co _ ( 2 ) atmosphere were tested on a bench scale fluidized bed facility. the characteristics of coal combustion and pollutant emission under o _ ( 2 ) / n _ ( 2 ) or o _ ( 2 ) / co _ ( 2 ) atmosphere were experimented on a circulating fluidized bed multi - function test - facility

    在熱天平上進行o _ 2 / n _ 2氣氛與o _ 2 / co _ 2氣氛下的煤焦熱解、著火與燃燼反應動力學及石灰石煅燒分解特性研究;在小型流化床試驗臺上進行石灰石在o _ 2 / co _ 2氣氛下的煅燒與硫化反應特性研究;在設計、搭建的循環流化床多功能綜合試驗臺上進行o _ 2 / n _ 2氣氛與o _ 2 / co _ 2氣氛下的煤燃燒特性與污染物排放規律研究。
  9. This paper is subject to national emphasized groundwork research item named conception validation about the new process of coal translation and optimization integration of the process, and it focuses on the research of the monitoring and controlling system of circulation fluidized bed ( cfb ) multi - generation test - bed according to the test - bed project of zhejian university institute of thermal power engineering cfb multi - generation system combining combustion & gasification test - bed, while considering an utilizing advanced technology and experience domestically and abroad

    本課題從屬于國家重點基礎研究規劃項目一煤轉化新過程概念驗證及過程的優化集成課題,結合浙江大學熱能工程研究所循環流化床燃燒氣化熱電氣多聯產試驗臺,根據試驗臺的實際情況,借鑒國內外的先進技術和經驗,對循環流化床多聯產試驗臺的計算機監控系統應用進行了深入的研究。
  10. Abstract : in the internal circulating fluidized bed, there exist the moving zone, fluidizing zone and heat transferring zone with different fluidized air velocities. the convection heat transfer coefficient of immersed tube in the heat transferring zone is impacted by the velocity of the moving zone nearby and its data and change trend are obviously different with those of the common bubbling bed. the maximum heat transfer coefficient is evidently higher than that of the bubbling bed. as the bed materials have not been fluidized in the heat transfer zone, the coefficient has increased highly. the curve of that changes gently, feasilble to control the combustion intensity in the fluidizing zone

    文摘:垃圾焚燒系統中,內旋流流化床存在不同布風速度的移動區、流動區和換熱區,處于換熱區的埋管的對流換熱系數受附近流動區氣流參數的影響,其變化趨勢及數值大小與普通鼓泡型流化床之間有明顯不同:最大的對流換熱系數明顯高於鼓泡床;換熱區尚未流化時,對流換熱系數已經大幅提高;整條換熱曲線的變化比較平緩,易於流化床濃相床內換熱。
  11. The boilers are well - structured and bring good benefit for enviroment protection. china is a big country for energy consumption, now, saving energy and enviroment protection have been already put on the importment order of the day. the quantity of the boiler required for the development of industry has been increasing, the annual requirement is about 100, 000steam - tons. recently, it has higher requirment to develop the thermoelectricity combustion production. therefore, 220ton hour circulation fluidized bed will have a good prospective market

    中國是一個能源消耗大國,現已將節約能源和保護環境,提到了重要日程,而工業的發展對鍋爐的需求量還在不斷增大,每年約需10萬蒸噸,且目前對發展熱電聯產有更高的要求,因此,生產220噸時循環流化床鍋爐有較好的市場前景。
  12. Based on simulation, 2 - dimension fuzzy control system was researched, which was used to control two correlative variables of circulating fluidized bed boiler " s combustion control system

    本論文在模擬的基礎上,研究用二維模糊控制實現流化床鍋爐燃料量控制系統的兩關聯變量的控制。
  13. Yth circulating fluidized bed boiler ' s sulfur capture effect can achieve to 89. 6 percent, the average of sulfur dioxide capture is 1060mg / m3, nitrogen oxide is 110mg / m3, dust of gas is 87 mg / m3. this suggests that cfb can achieve the standard of clean combustion

    雲天化循環流化床鍋爐循環流化床鍋爐的脫硫效率達到89 . 6 、 so _ 2平均排放量為1060mg m ~ 3 , no _ x的平均排放量為110mg m ~ 3 ,煙氣中粉塵平均排放量為87mg m ~ 3 ,證明了循環流化床鍋爐達到了潔凈燃燒的標準。
  14. Circulating fluidized bed ( cfb ) combustion technology is a new efficient and clean combustion technology. its application is of great significance to china for the reasons of economical and environmental benefits in the recent years. great progress has been made in the theory of cfb these years

    循環流化床( cfb )燃燒技術作為新一代高效、低污染清潔燃燒技術,其近年來的廣泛推廣和應用帶來了重大的經濟和環境效益,同時循環流化床理論也得到了很大的發展和進步。
  15. Circulating fluidized bed boiler ' s combustion efficiency is very high, and it ' s value of economic and environment protection is superior to other type boiler. so it is worth for us to spread circulating fluidized bed boiler

    循環流化床鍋爐的燃燒效率很高,大於或等同於煤粉爐,其經濟和環保價值均優于其他類型鍋爐,因此它是個值得大力提倡推廣的燃煤爐型。
  16. Part of content about fluidized bed thermodynamic calculation in the 《 layer and fluidized combustion thermodynamic calculation standard for industrial boiler 》 ( jb / dq1060 - 83 ) are discussed the computing equation of fly ash carbon content and the thermal equilibrium equation in the dense phase considering evaporation of water of unburned coal are given. the revise necessary is provided through calculating examples

    對jb / dq1060 - 83 《層狀燃燒及沸騰燃燒工業鍋爐熱力計算標準》中沸騰爐熱力計算的部分內容進行了探討,導出了沸騰層飛灰含碳量計算式和考慮未燃煤水分蒸發的沸騰層熱平衡方程,通過算例說明了修正的必要性。
  17. The heat balance equations on incineration of organic liquid waste in fluidized - bed incinerator with coal as auxiliary fuel is established in this paper. the relations between the feeding rate of auxiliary fuel and the lhv of liquid waste, the incineration temperature, and the preheated combustion air temperature have been discussed. this paper also discussed the relation between the lhv of liquid waste and combustion air temperature as the auxiliary fuel is not necessary, and provides the theoretical foundation for the design and operation on fluidized - bed incinerator

    建立了以煤為輔助燃料的,有機廢液在流化床中焚燒的熱平衡方程,求得輔助燃料耗量與各影響因素的計算式,得出輔助燃料耗量與廢液中可燃基的低位發熱值、密相區燃燒溫度、熱風溫度之間的關系曲線,以及不需要輔助燃料時,有機廢液熱值與熱風溫度之間的關系,為流化床焚燒爐的設計與運行提供了理論依據。
  18. A part of content about fluidized bed thermodynamic calculation in the 《 layer and fluidized combustion thermodynamic calculation standard for industrial boiler 》 ( jb / dq1060 - 83 ) are discussed the computing equation of fly ash carbon content and the thermal equilibrium equation in the dense phase considering evaporation of water of unburned coal are given. the revise necessary is provided through calculating examples

    對jb / dq1060 - 83 《層狀燃燒及沸騰燃燒工業鍋爐熱力計算標準》中沸騰爐熱力計算的部分內容進行了探討,導出了沸騰層飛灰含碳量計算式和考慮未燃煤水分蒸發的沸騰層熱平衡方程,通過算例說明了修正的必要性。
  19. The combustion conditions in a circulating fluidized bed ( cfb ) boiler are much different from a pulverized coal firing ( pf ) boiler. however, this dissertation has confirmed that coal char in cfb boiler will also experience reactivity loss and ordering of turbostratic carbon structure, which have been reported by many researchers whose work were mainly restricted to pf conditions

    本文通過獲得在cfb燃燒條件下熱解和燃燒過程中的焦碳,對其反應性、亂層碳結構、礦物質催化作用和比表面積等進行了系統研究,指出cfb鍋爐和煤粉爐同樣存在焦碳亂層碳結構有序化和焦碳反應性下降(失活)現象,並全面分析了焦碳失活的機理。
  20. Coal partial gasification combined cycle generation is a kind of technology combined coal gasification and fluidized - bed combustion, which is fit for the situation of our country

    煤部分氣化聯合循環發電系統是一種把煤氣化技術和流化床燃燒技術結合起來的適合我國國情的聯合循環發電技術。
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