首页 | 本学科首页   官方微博 | 高级检索  
文章检索
  按 检索   检索词:      
出版年份:   被引次数:   他引次数: 提示:输入*表示无穷大
  收费全文   190篇
  免费   3篇
  国内免费   6篇
安全科学   89篇
废物处理   2篇
环保管理   16篇
综合类   14篇
基础理论   13篇
污染及防治   12篇
评价与监测   3篇
灾害及防治   50篇
  2023年   2篇
  2022年   2篇
  2021年   7篇
  2020年   16篇
  2019年   4篇
  2018年   1篇
  2017年   4篇
  2016年   5篇
  2015年   15篇
  2014年   8篇
  2013年   6篇
  2012年   5篇
  2011年   9篇
  2010年   2篇
  2009年   8篇
  2008年   4篇
  2007年   1篇
  2006年   6篇
  2005年   5篇
  2004年   3篇
  2003年   7篇
  2002年   1篇
  2001年   6篇
  2000年   3篇
  1999年   3篇
  1998年   4篇
  1997年   8篇
  1996年   6篇
  1995年   19篇
  1994年   6篇
  1993年   5篇
  1992年   2篇
  1991年   4篇
  1990年   3篇
  1987年   3篇
  1986年   1篇
  1985年   3篇
  1984年   1篇
  1980年   1篇
排序方式: 共有199条查询结果,搜索用时 31 毫秒
1.
The radiant heat flux from a pool fire is frequently calculated using the solid flame model, where the flame envelope is approximated as a stationary cylinder whose surface emits thermal radiation at a constant rate. Radiant heat flux calculations using the solid flame model assume the target to be at a given elevation, typically at ground level, and to have an unobstructed view of the fire. The presence of obstacles (e.g., walls, buildings, etc.) or terrain features that would create shaded areas and provide shielding of a target from the fire is typically neglected in these calculations: this is a conservative approach, but it is not accurate. This paper presents a methodology to utilize the solid flame model to calculate the heat flux to a target while taking into account the presence of an obstruction between the target and the fire. The shielded solid flame method can quantitatively account for the presence of obstacles as a passive mitigation measure and allows project developers or designers to optimize their facility layout to meet safety requirements. The methodology presented in this paper uses the same correlations found in currently used solid flame models (e.g., LNGFIRE3), therefore, it remains consistent with current regulatory requirements for LNG facilities in the U.S.  相似文献   
2.
Thermal runaway hazard assessment provides the basis for comparing the hazard levels of different chemical processes. To make an overall evaluation, hazard of materials and reactions should be considered. However, most existing methods didn't take the both into account simultaneously, which may lead the assessment to a deviation from the actual hazard. Therefore, an integrated approach called Inherent Thermal-runaway Hazard Index (ITHI) was developed in this paper. Similar to Dow Fire and Explosion Index(F&EI) function, thermal runaway hazard of chemical process in ITHI was the product of material factor (MF) and risk index (RI) of reaction. MF was an indicator of material thermal hazards, which can be determined by initial reaction temperature and maximum power density. RI, which was the product of probability and severity, indicated the risk of thermal runaway during the reaction stage. Time to maximum rate under adiabatic conditions and criticality classes of scenario were used to indicate the runaway probability of the chemical process. Adiabatic temperature rise and heat of the desired reaction and secondary reaction were used to determine the severity of runaway reaction. Finally, predefined hazard classification criteria was used to classify and interpret the results obtained by this method. Moreover, the method was validated by case studies.  相似文献   
3.
To explore the reaction thermodynamics of a styrene-ethylbenzene mixed system, a differential scanning calorimetry (DSC) analysis was performed on the mixed system with styrene: ethylbenzene mass ratios of 1:0, 4:1, 3:2, and 2:3 at heating rates of 2.5, 5, 7.5, and 10 K/min. The activation energy of the mixed reaction system was calculated using the model-free Kissinger kinetic method, to determine a mixed system of relative stability mixing proportion. The thermodynamic parameters of the styrene-ethylbenzene mixture system at the optimal ratio were obtained using an adiabatic accelerating calorimeter. Further, dynamic thermal parameters such as the activation energy of the hybrid system, pre-exponential factor and order of reaction, TMR, TMRad, and TD24 were calculated.  相似文献   
4.
为预防输气站降压排污过程中发生事故,提出1种基于2GW-HAZOP与偏离度的作业过程风险评估方法。在HAZOP方法的基础上定义作业偏差,将传统7种工艺参数偏差引导词映射到1个偏差二元组中;通过将作业过程节点功能作为参量,采用节点跨越和节点功能偏离2种引导词,从而构建节点功能偏差;进一步通过定义功能偏离度和控制措施偏离度对偏差进行量化处理,表征风险水平;将方法应用于降压排污作业过程的风险评估中,可分析得到偏离度大的作业过程节点。结果表明:分离器放空不充分、排污池液位过高或过低、排污结束未检查泄漏情况的偏离度较大,需加强风险控制。  相似文献   
5.
Former methods used in the U.S. to assess hazardous and explosible coal dust date back to the 1950s. As mining technologies advanced, so too have the hazards. Given the results of the recent coal dust particle size survey and full-scale experimental mine explosion tests, the National Institute for Occupational Safety and Health (NIOSH) recommended a new minimum standard, in the absence of background methane, of 80% total incombustible content (TIC) be required in the intake airways of bituminous coal mines, replacing the previous 65% TIC requirement. Most important to monitoring and maintaining the 80% TIC is the ability to effectively collect and analyze representative dust samples that would likely disperse and participate in dust explosion propagation. Research has shown that dust suspended on elevated surfaces is usually finer, more reactive, and more readily dispersible while floor deposits of dust are generally coarser and more difficult to disperse given the same blast of air. The roof, rib, and floor portions of the dust samples were collected and analyzed for incombustible content separately and the results were compared to a band sample of the roof, rib, and floor components. Results indicate that the roof and rib dust samples should be kept separate from floor dust samples and considered individually for analyses. The various experimental collection methods are detailed along with preferred sampling approaches that improve the detectability of potentially hazardous accumulations of explosible dust.  相似文献   
6.
超过12m的超高中庭发生火灾时,常规排烟方法不能完全满足实际需求。通过FDS软件对某超高"Z型"中庭进行数值模拟,研究中庭高度对自然排烟特性的影响。该"Z型"中庭底层南面是自然进风口,顶层北面是自然排烟口,以烟气最先到达指定楼层人员危险时间值为到达危险时间。实验条件下模拟结果表明:无风情况下,中庭高度增加,到达危险时间增加,自然排烟效果增强。到达危险时间t与中庭高度h之间满足一定指数增长关系:t=y0+Aexp(h/α),中庭火源位置和中庭宽度对y0、A和α有一定影响。有风情况下,外界风向与进风口方向一致时,中庭自然排烟效果优于无风状况,中庭越高效果越强。在外界风向与排烟口方向相反时,烟气倒灌进中庭,自然排烟效果较弱。  相似文献   
7.
伴随我国经济发展的进步,虽然农村的生活水平得到一定的改善,但是并没有根据实际情况将相关生态处理技术应用,导致农村污水处理的效率无法有效的提升,严重影响农村的发展。基于此,本文主要分析了农村生活污水处理的方式,以及污水处理不当对人们的危害与影响,并阐述了农村污水处理的主要对策与方案,笔者根据自身经验提出相应的建议与意见。  相似文献   
8.
赵鹏程  姚斌 《火灾科学》2020,29(1):63-70
机场航站楼公共区域多采用自然排烟方式,而环境风和排烟窗控制模式会影响排烟效果,尤其在弧形立面航站楼中影响效果显著。以某弧形立面航站楼为研究对象,选取候机指廊弧形区域的自然排烟窗分3段控制启闭,进而确定6种控制模式,采用 FDS火灾动力学模拟软件研究了不同模式下的排烟效果,获得了环境风和发烟量对危险到达时间的影响规律, 提出了排烟窗控制模式流程。结果表明:对于弧形立面航站楼而言,排烟窗分段控制模式下的排烟效果优于不分段控制模式,可以有效降低环境风对自然排烟的影响。当环境风速超过10 m/s时,须关闭迎风向排烟窗,避免烟气倒灌。在法向环境风作用的不利条件下,当发烟量在0. 05~0. 20之间时,危险到达时间的最大值tmax与发烟量x满足一次函数关系式:tmax=-3018x+1030.5。  相似文献   
9.
Most process hazard analysis (PHA) studies today are conducted using traditional methods such as the hazard and operability study (HAZOP). Traditional methods are based on a chain-of-events model of accident causality. Current models of accident causality are based on systems theory and provide a more complete representation of the causal factors involved in accidents. Consequently, it is logical to expect that PHA methods should reflect these models, that is, system-theoretic hazard analysis (STHA) should be used. Indeed, system-theoretic process analysis (STPA) has been developed as such a method. STPA has been used in a variety of industries but, at this time, it has not gained acceptance by the process industries. This article explores the reasons for this situation. Expectations for PHA in the process industries are examined and issues for the application of STPA in the process industries are discussed. It is concluded that a variety of matters must be addressed before STPA can be considered as a viable PHA method for the process industries and the case for the use of STHA in the process industries is not yet proven.  相似文献   
10.
Identifying dead-legs and related corrosion issues continues to be a challenge in the process industry. Pipeline corrosion has been a factor in several recent incidents involving releases and fires. A review of incident reports and citations over the past ten years indicates that Process Hazard Analysis (PHA) revalidations have been noted for not addressing the hazards of a process including corrosion mechanisms and dead-legs. In order for the hazards to be addressed, they must first be accurately identified in a PHA and documented along with any recommended actions for preventive maintenance. This paper describes a methodology for identifying and addressing dead-legs and related corrosion issues in a PHA that can be used to update corporate PHA procedures to be more robust in preventing corrosion related incidents.  相似文献   
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号