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详细信息

电动执行器钢性防火罩

JSAVE柔性防火罩是工厂管理中一种有效保护设备的措施,它能将炼油厂、石油平台、石油化工、热电站、电器、造船厂和军工等场所因火灾而产生的危害与损失降至Z低

的详细信息

夹克:柔性护套钢外壳:钢箱4.FR Board : Intumescent Fireproofing Board

3.FR Steel Enclosure : Steel Box

The products was tested in fire laboratories as the time-temperature curve of UL1709
(rapid rise fire tests of protection materials).
The time-temperature curve of UL1709 is severe hydrocarbon fire curve which is possible to occur in refinery,
petrochemical and off shore platform.
The valve actuators should proof for the period of 30 minutes operation under UL1709 fire time-temperature curve.

产品测试实验室为ul1709火的温度时间曲线

(rapid rise fire tests of protection materials).

防护材料的快速上升试验。

The time-temperature curve of UL1709 is severe hydrocarbon fire curve which is possible to occur in refinery,

ul1709的时间温度曲线是严重的烃类火灾曲线这是可能发生在炼油厂,

petrochemical and off shore platform.

石化和离岸平台。阀门执行机构应为ul1709火灾升温曲线下30分钟运行周期的证明。

海洋平台爆炸试验与研究,喷射火试验为iso22899 1 is required Intumescent coating we manufactured was tested for 2.0 bars blast and J-90 jet fire in Advantica, Cumbria, UK.

我们的制造业是膨胀型涂料测试为2.0J - 90酒吧爆炸喷射火

纤维素火点火后有缓慢的火焰温度上升.。标准的纤维素火灾温度与时间曲线应是参考文献:BS476IMO决议A51713),ISO r834和国际海上人命安全公约。典型的辐射值5分钟后点火为50千瓦/平方米。

纤维素火灾温度与时间曲线的美国(ASTM E119nfpa251ul263)稍快。

Hydrocarbon fire

烃类火灾A hydrocarbon fire has a rapid flame temperature rise after ignition. The standard hydrocarbon fire碳氢化合物火灾燃烧后火焰温度迅速上升。标准烃火 temperature vs. time

温度与时间曲线应是BS476 20ul1709。典型的稳态温度为1100 oCcurve shall be that of BS476 Part 20 and UL1709. Typical steady-state temperature is 1100 oC.

Typical radiation value 5 minutes after ignition is 160 kW/m2.

典型的辐射值5分钟后点火为160千瓦/平方米。喷射火 Jet fire

Jet fire is a turbulent diffusing flame, resulting from the combustion of a steady release of pressurised liquid

喷火是湍流扩散火焰,一个稳定的释放加压液体燃烧产生的

or gaseous fuel. They are the most severe fire scenario that PFP materials could be required to withstand,

或气态燃料。他们是亲民的材料可能需要承受最严重的火灾场景,

considering the effect of erosion and also the significantly higher rate of burning due to turbulent fuel air mixing.

考虑到侵蚀的影响,也显着较高的燃烧率,由于湍流燃料-空气混合。

Test procedure shall be of ISO 22899-1.

测试程序将ISO 22899-1。爆破试验 Blast test

典型的最大阻力为对象的表面面积小,如结构构件

assumed to be 0.2 to 1.0 barg.

假定是0.21巴。

PFP systems shall have demonstrable explosion resistance that can be supported by relevant testing.

Preference shall be given to systems that have been subjected to dynamic explosion testing by a recognised independent establishment.

对认可的独立机构进行动态爆炸试验的系统,应给予优先考虑。The valve actuators should proof for the period of 30 minutes operation under UL1709 fire time-temperature curve.

1.1 These requirements describe a test method measuring the resistance of protective materials to rapid-temperature-rise fires.

1.1 本文规定了一个量测防护材料在快速升温火环境下耐火性能的实验方法.

1.2 The test method covers a full-scale fire exposure, intended to evaluate the thermal

resistance of protective material applied to structural members and the ability of the protective material to withstand the fire exposure.

1.2 实验方法包含一个全尺寸火灾实验,用来评价应用于结构构件的防护材料的耐热性能和耐火性能.

1.3 The test method also covers a small-scale fire exposure, intended to evaluate the ability of protective materials to withstand a variety of environmental conditions anticipated.

1.3实验方法同时也包含了一个小比例火灾实验,用来评价防护材料在多种预期环境下的耐受能力.

2 General

2.总则

2.1 Units of measurement

2.1计量单位

2.1.1 Values stated without parentheses are the requirement. Values in parentheses are explanatory or approximate information.

2.1.1 未加括弧的数值为精确值,加注括弧的为解释值或近似值.

2.2 Undated references

2.2没有标注日期的内容

2.2.1 Any undated reference to a code or standard appearing in the requirements of this standard shall be interpreted as referring to the latest edition of that code or standard.

2.2.1 在本标准中出现的任何没有标注日期的准则或规范都可认为是参照最新版本的准则或规范。

FULL-SCALE TEST METHOD

足尺寸实验方法

3 Furnace Control

3加热炉(马福炉?)控制

56°C) within 5 min from the start of the test. The fire environment is to be controlled by reproducing the furnace temperatures recorded during the furnace calibration method specified in Furnace Calibration, Section 4. This temperature is to be maintained throughout the remainder of the fire test as shown in Figure 3.1.±100°F (1093 ±16 kW/m2) and an average temperature of 2000 ±5000 Btu/h·ft2 (204±3.1 The fire environment within the furnace is to develop a total heat flux of 65,000

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