h scope 中文意思是什麼

Bussiness scope : cargo transportation mainly including cargo transportation ( includes superlonger, superwidt - h, superhigher, retail and entire, container cargo transportation ), dangerous cargo transportation ( includes flam - mability, blast, dangerous cargo transportation ) : international cargo transportation agent mainly undertake ocean shipping, land shipping, air shipping, inclduing : storage, transfer, container install and remove, ( our company has the specisl base for install and transfer remove the container ) ; our international foreign trade mainly in textile garments, light industry, electric engine, metals, chemical products inport and export ; for more we also undertake import materials for machining, compound of imported parts and import samples for producing etc

業務范圍：貨物運輸主要有普通貨物運輸（包括超長、超寬、超高、笨零、整零、整車、集裝箱貨物運輸） 、危險貨物運輸（包括易燃、易爆、危險品運輸） ；國際貨運代理主要承辦海運、陸運、空運進出口貨物的國際運輸代理業務，包括：倉儲、中轉、集裝箱拼裝拆箱（公司在上海港口設立專用倉儲、中轉、集裝箱、拼裝拆箱基地） ；國際貿易主要開展紡織服裝、輕工、機電、五金、化工等商品的進出口貿易；另外承接來料加工、來件裝配、來樣定貨的三來一補業務。

In mfc01dlg. h, go to the declaration of the dialog class, and add a data member for the user control in protected scope as follows

在mfc01dlg . h中，轉到對話框類的聲明，並添加受保護范圍內的用戶控制項的數據成員，如下所示：

H. d. lasswell, “ the policy orientation, ” in lerner and lasswell, ed., policy science : recent developments in scope and method, stanford university press, 1951

見張金馬主編， 《政策科學導論》 ，中國人民大學出版社， 1992年版，第1 2頁。

This text completely and systematically studies the status and the development of the pyrolysis and the fluidization of biomass, which distill the bio - oil in the domestic and international area, as well as the existing problems. this thesis primarily include following aspects : ( l ), by experimenting and measuring the energy ( heat value ) and the content of c, h, n chemical element of right 20 kinds of common biomass, on the base of the experimental result, and respectively established the biomass energy predict experiment formula with the element of h and c is from change, and passed the ro. os examination, which provides the basis and convenience for flash pyrolysis fluidization device energy to convert the rate to compute with biomass energy utilization calculation ; ( 2 ), proceeded the tg and dtg experimentation equal velocity ( 10 ? / min, 20 ? / min, 40 ? / min, 60 ? / min ) heating and constant temperature heating by studying on eight kinds of biomass samples, according to the experimental data and arrhenius formula, we established the dynamics model of pyrolysis of, then, using the goast - redfern and p function, we also solved the dynamics parameters and analyze out every kind of biomass ' s frequency factor and parameters of activation energy, and established the every kind of dynamics model of pyrolysis of biomass, all of these provide the theories and basis to make sure the reactor ' s flash pyrolysis work temperature scope design and the describing of pyrolysis reactor dynamics ; ( 3 ), in order to study and ascertain the process of heat completely getting to pyrolysis time of varied size biomass particles, we observed and measured the ratio of length and diameter ( l / d ) with the varied biomass through electron microscope, we concluded the l / d ratios usually is from 5. 0 to 6. 0, the average is 5. 3 ; ( 4 ), we studied the process of biomass transiting and the theory of complete pyrolysis time with the theory of complicated heat field, we got the time ( t ) of the varied size biomass particles arriving to complete pyrolysis, and we knew that the complete pyrolysis time and the time which get to the biggest production ratio are identical, all of these studies provide the theory base for design and forecasting the flash pyrolysis reactor solid state resort time ; ( 5 ), according to the above experiment result, synthesize to make use of the engineering the mechanics, engineering the material, machine the design to learn the principle, deduce, establish the theory of rotation cone flash pyrolysis reactor material resort time ( t ) and reasonable rotation velocity ( or frequency ) relation theory ; and ( 6 ), we gave the reactor ' s smallest cone angle certain, reactor cone wall strength design theory, the reactor production ability theory, the power design method and the critical rotation velocity theory

本文較全面、系統地綜述了國內外生物質熱解液化制取生物燃油技術研究發展現狀及存在的問題，主要研究內容有： （ 1 ）實驗、測定了20種常見生物質的能量（發熱量）和c 、 h 、 n元素含量，根據實驗結果分別建立了以h和c為自變量的生物質能量預測經驗公式，並通過r _ （ 0 . 05 ）檢驗；為閃速熱解液化裝置能量轉化率計算和生物質能量利用率計算提供了依據和方便； （ 2 ）選擇了8種生物質試樣作了等加熱速率（ 10 min 、 20 min 、 40 min 、 60 min ）和恆溫加熱的tg和dtg實驗，根據實驗數據和阿倫尼烏斯公式建立了生物質熱解反應動力學微分方程，並採用goast - redfem積分法和p函數對其動力學參數進行了求解，解析出各種生物質的頻率因子和活化能參數，進而建立了各種生物質的熱解動力學模型，為科學確定反應器的閃速熱解工作溫度范圍及熱解反應動力學描述，提供了理論和依據； （ 3 ）為研究和確定不同尺度的生物質顆粒中心達到全熱解的時間，在體視顯微鏡下對不同粒度的生物質顆粒的長徑比進行了實驗觀察和測定，得出生物質的長徑比（ l d ）一般在5 . 0 6 . 0之間，平均為5 . 3的結果； （ 4 ）採用復雜溫度場傳熱學理論對生物質傳熱過程及充分熱解時間理論進行了研究，解析推導出了不同尺寸生物質顆粒中心溫度達到充分熱解溫度的時間（ t ） ，得出了理論推導的充分熱解時間與最大產油率的熱解時間相一致的結果，為閃速熱解反應器固相滯留時間設計和預測提供了理論依據； （ 5 ）根據上述實驗結果，綜合運用工程力學、工程材料、機械設計學原理，推導、建立了轉錐式閃速熱解反應器物料滯留時間（ ）與轉速（或頻率）合理匹配理論； （ 6 ）提出了轉錐式閃速熱解反應器的最小錐角設計、錐壁強度設計、生產能力設計理論和功率計算方法及臨界轉速理論等。

The second part ( chapter two ) : by describing the concept and characters of h the risk ; by describing the essence and the process of the risk management ; by giving a clear definite of " the asset evaluation risk ", explaining its character, inducing the views concerning the risk categories at the same time, in the last, introducing the leading actor - " risk management of asset evaluation ", and discussing its quality and its scope

第二部分（第二章） ：明確了風險的含義、屬性及其特徵，以此為理論基礎，指出了當前有些觀點存在的不足之處，對資產評估風險的本質、特點作了清晰的界定；通過介紹風險管理的本質、內容及操作程序，說明了「資產評估風險管理」的性質及其系統層次結構，為全文的展開做了理論鋪墊。

Then virtual dielectric constant method is adopted to calculate the electric field distribution with floating electrodes, and equivalent conductance rate method is adopted to calculate the electric field distribution with surface filth or local puncture in the insulator, furthermore the value scope of virtual conductance rate and equivalent conductance rate are discussed and some useful results are got. for the solution of vortex loss of silicon steel sheets concerning current transformer, the h solution has also been put forward rather than traditional a ? ( p method in order to reduce calculation load

採用虛擬介電常數法計算絕緣子存在懸浮導體的電場分佈，採用等效電導率法計算絕緣子存在表面污穢或局部擊穿情況下的電場分佈。對虛擬介電常數和等效電導率的取值范圍進行了討論，得出了一些有用的結論。對于電流互感器硅鋼片渦流損耗的計算，本文提出了不同於傳統的a -方法的h求解辦法，從而大大簡化了計算。