heat recovery 中文意思是什麼

heat recovery 解釋
廢熱回收
  • heat : n 1 熱;熱力;熱度;熱量。2 體溫;發燒。3 (氣候的)高溫,暑氣。4 【冶金】熔煉的爐次;裝爐量;一...
  • recovery : n. 1. 重獲;復得;恢復,收回,回收。2. 還原,復原;痊癒;蘇生;矯正。3. 回縮。4. 填地。5. 【法律】勝訴。
  1. Surplus heat recovery of gas engine driven water to water heat pump

    水燃氣機熱泵的余熱回收
  2. Cast iron melting furnaces and related facilities, waste heat recovery system

    鑄鐵溶解爐鑄鐵熔爐相關設備,廢熱回收系統
  3. The manufacturing program includes ventilating, air - conditioning and heat recovery plants, surface technology, industrial fans and recycling systems and plants with the aim of environmental protection as well as dust collection plants

    歐德通風的製造范圍包括通風,空氣調節,熱回復設備,表層處理,離心風機以及針對于環境保護的垃圾回收設備。
  4. In the third, this paper makes a survey on components of the exhausted flue gas and waste heat resource, and discusses the possibility and methods of steam generation and air preheating with the waste heat. and then, the analysis on the advantages and disadvantages of heat recovery plants with conventional steel - water heat pipes and inorganic heat - transfer heat pipes is carried out. the paper also gives a valuation about the plan and features of the design of heat recovery

    對余熱源排煙的成分和余熱資源量進行標定,討論余熱回收產生蒸汽或加熱燃燒用空氣的可行性和方法,分析常規余熱回收技術設計、採用普通鋼-水熱管和無機傳熱熱管等傳熱元件的設計余熱回收裝置的優缺點,並對余熱回收設計方案及其特點進行總體評價。
  5. Using the opened thermosiphon of 38x3 as experimental element and water as working fluid, the characteristics of dynamic low load boiling, stable severe boiling heat transfer coefficient and critical heat flux are gotten for the opened thermosiphon at the pressure of 0. 02 - 0. 1mpa and 0. 1 - 0. 8mpa respectively, which makes up the drawback that the opened thermisiphon has not yet accurate boiling heat transfer relationship formulas. by means of experimental results, an opened thermisiphon waste heat recovery boiler is designed for the high temperature gases that the positi e electrode copper refining furnace exhaust, which overcomes effectively the drawback of short life, little capacity and unable to inspect that the closed steel - water thermosion has

    本文以工程上常用的38 3的開口封底為實驗元件,以水為工質,對開啟式熱管內的動態低負荷沸騰、穩態旺盛沸騰及臨界沸騰特性進行系統的可視化實驗研究,實驗壓力為0 . 02 0 . 8mpa ,實驗得出了38 3的開口封底管在工作壓力為0 . 02 0 . 8mpa和0 . 1 0 . 8mpa下的管內沸騰傳熱系數及臨界熱負荷計算關聯式,彌補了開口封底管? ?這一新型傳熱元件尚無準確的沸騰換熱關聯式的缺陷。
  6. 2. design scheme of gravity heat pipe air pre - heater is proposed which fits the actual situation of injecting steam boilers. detailed heat calculation and design on heat recovery of flue gas is carrying out

    提出了採用適合於注汽爐實際工況的重力熱管式空氣預熱器的設計方案,對煙氣的余熱回收進行了詳細的熱力計算和設計。
  7. The second chapter studies the economy of ship ' s power plants, based on the aspects of lowering fuel cost, waste heat recovery, the match of ship, machinery and propeller, increasing propulsion efficiency, increasing the economy of ship ' s power plants, etc. the third chapter discusses in detail the control measures of voyage change cost, analysizes systematically the voyage change cost based on the way of fuel cost, harbor cost, voyage venture cost. the fourth chapter studies the structures and control measures of seafarers cost, maintenance cost, spare parts and stores cost, lubricating oil cost, etc. which are relatively easy to be controlled ; based on the state maintenance decision - making, a mathematical model is put forward, the validity and its solve process are discussed. the control measures of spare parts, fuel cost and lubricating oil cost should be based on scientific budget, through the control means of application, reception, usage, store check, try to acquire the inosculation of theory

    第一章主要討論營運船舶運輸成本,對船舶運輸成本的概念、結構、性質與分攤、成本細分進行了分析,從宏觀上闡明了船舶運輸成本的生存環境和生長趨勢;第二章研究了船舶動力裝置的經濟性,在營運船舶降低油耗、廢熱利用、船機槳匹配、提高推進效率、提高船舶動力裝置經濟性的有效途徑等方面進行了闡述和論證;第三章詳細論述並論證了航次變動成本的控制措施,全面系統地分析和總結了航次變動成本,通過對燃油成本、港口使費、航次風險成本的分析與控制,提出了航次風險成本的概念並論述了若干航次風險成本的控制措施;第四章對船舶營運成本中的船員費用控制、維修保養及其費用控制、船舶備件物料管理及其費用控制等幾個主要可控性較高的成本進行了細致的分析並分別討論了相互的控制措施,提出了基於狀態維修決策的馬爾可夫數學模型並論證了模型的正確性及具體解算步驟,對于備件、燃潤物料的控制堅持以科學的預算為前提,以申領、接收、使用、盤存為控制環節,切實做到理論與實踐的密切結合;第五章,結合營運成本的預核算的案例,對船舶營運成本的預算及核算進行了有益的探討,旨在揭示成本發生的動因,並給出了成本預算、核算的編制方法。
  8. High - efficiency heat recovery is the key benefit of mechanical ventilation over conventional natural ventilation

    有效地抵禦熱量是機械通風相對于傳統的自然通風最重要的優勢。
  9. For saving energy with waste heat recovery thermo - acoustic engine is a promising way due to its simple structure, absence of pollution and low cost

    摘要以低溫排熱的有效利用為目的,設計製作了一臺熱聲發動機的實驗樣機。
  10. Often supplied as turnkey equipment packages, systems can include heat recovery, gas preheating and downstream tail gas clean - up as required

    經常提供交鑰匙的整套設備系統可以根據需要包括熱回收、氣體預熱和下游的尾氣凈化。
  11. In chapter 5, the principle of molten carbonate fuel cell power system is introduced. the development of the system, such as the improvement of cell components including electrodes and electrolyte, the fuel processing, the heat recovery, the power conditioning and grid interconnection, the control system and the combine generation

    第五章在簡要敘述了熔融碳酸鹽燃料電池發電系統原理后,從以下幾個方面對系統的開發進行了論證:單體元件(電極和電解質)性能的提高,燃料的處理,余熱利用,電力調節和並網,燃料電池/燃氣輪機/汽輪機聯合發電以及系統控制與優化。
  12. Ventilation for buildings - performance testing of components products for residential ventilation - performance testing of a mechanical supply and exhaust ventilation units including heat recovery for mechanical ventilation systems intended for single family dwellings

    建築物的通風.住宅通風用部件產品的性能試驗.獨戶住宅機械通風系統用機械供氣和排氣通風裝置
  13. The temperature of inlet air could be raised by the developed heat recovery device to achieve energy saving

    加熱器的耗油率為4 . 5公升小時,分析進氣的溫升和流量可得此乾燥系統之加熱爐的加熱效率約為50 % 。
  14. Gas turbine heat recovery steam generators

    燃氣輪機熱回收蒸汽發生器
  15. There are many kinds of methods dealing with fresh air supplying, such as free fresh air supplying, fresh air sucking, independent fresh air supplying, heat recovery ventilating ( hrv ), etc. it was proved that ac equipment capability and iaq has a relationship with fresh air states in fan - coiling and fresh air system

    除了無組織的新風供應方式,住宅空調系統新風供應還有新風吸入方式、獨立新風供應、新風換氣機方式。風機盤管加新風系統中,新風處理到不同的狀態點,對空調設備負擔的負荷及室內空氣狀態都有影響,本文對各種新風處理狀態進行了分析。
  16. Improvements of this process will probably be tied to more efficient heat recovery arrangements.

    此方法的改進看來是要致力於更有效的熱量回收措施。
  17. Abstract : the causes for low efficiency of the heater in no. 2 crude unit of jpc refinery are described and analyzed including water leaking of steam soot blower, dew point corrosion caused by steam, soot deposits in convection chamber owning to poor soot blowing, high flue gas temperature, no heat recovery of flue gas, and poor performance of insulation lining, etc. by using sonic soot removing system, flue gas recovery system, spray coating of fiber and rock wool, as well as adjustment of flow scheme accordingly in the technical revamping. the dew point corrosion is completely eliminated, the insulation performance is improved, the heat loss is reduced by 1. 25 %, the flue gas temperature is reduced to about 170, and the heater efficiency is increased from 83 % to more than 90 %

    文摘:分析了金陵石油化工公司煉油廠二套常減壓裝置加熱爐存在的因蒸汽吹灰器漏水,蒸汽引起露點腐蝕及吹灰效果差造成對流室積灰,排煙溫度高,煙氣熱量未回收利用以及爐子保溫襯里效果差等問題,提出採用聲波除灰系統、煙氣回收系統、纖維噴塗和巖棉噴塗及相應的流程調整等改造措施.測定結果表明,本次技術改造解決了因蒸汽吹灰器漏水所造成的露點腐蝕問題,提高了保溫效果,減少散熱損失1 . 25 % ,排煙溫度降至170左右,裝置的爐效率由83 %左右提高到90 %以上
  18. The causes for low efficiency of the heater in no. 2 crude unit of jpc refinery are described and analyzed including water leaking of steam soot blower, dew point corrosion caused by steam, soot deposits in convection chamber owning to poor soot blowing, high flue gas temperature, no heat recovery of flue gas, and poor performance of insulation lining, etc. by using sonic soot removing system, flue gas recovery system, spray coating of fiber and rock wool, as well as adjustment of flow scheme accordingly in the technical revamping. the dew point corrosion is completely eliminated, the insulation performance is improved, the heat loss is reduced by 1. 25 %, the flue gas temperature is reduced to about 170, and the heater efficiency is increased from 83 % to more than 90 %

    分析了金陵石油化工公司煉油廠二套常減壓裝置加熱爐存在的因蒸汽吹灰器漏水,蒸汽引起露點腐蝕及吹灰效果差造成對流室積灰,排煙溫度高,煙氣熱量未回收利用以及爐子保溫襯里效果差等問題,提出採用聲波除灰系統、煙氣回收系統、纖維噴塗和巖棉噴塗及相應的流程調整等改造措施.測定結果表明,本次技術改造解決了因蒸汽吹灰器漏水所造成的露點腐蝕問題,提高了保溫效果,減少散熱損失1 . 25 % ,排煙溫度降至170左右,裝置的爐效率由83 %左右提高到90 %以上
  19. After fully heat - exchanged inner individual processes, the further integration for heat sources and heat sinks of processes with utility system of steam - power cogeneration was made, including the balance between energy use and heat recovery, cogeneration of steam and power, optimization of steam levels, and synthesis of turbine networks

    在實現各過程內部熱量交換的基礎上,進行各過程之間的剩餘熱阱和熱源與蒸汽動力系統的全局能量集成,包括廢熱回收、熱功聯產、蒸汽系統設計和透平網路綜合。
  20. Heat pumps, thermal storage, waste heat recovery, low - energy process equipment

    熱泵、熱能儲存、廢熱回收、低耗能加工設備
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