推薦產品
等級
standard
存貨情形
available only in Japan
濃度
100 mg/dL
SMILES 字串
Oc1ccccc1
InChI
1S/C6H6O/c7-6-4-2-1-3-5-6/h1-5,7H
InChI 密鑰
ISWSIDIOOBJBQZ-UHFFFAOYSA-N
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訊號詞
Warning
危險聲明
防範說明
危險分類
Met. Corr. 1
儲存類別代碼
8B - Non-combustible corrosive hazardous materials
水污染物質分類（WGK）
nwg
閃點（°F）
Not applicable
閃點（°C）
Not applicable
個人防護裝備
Faceshields, Gloves, Goggles, type ABEK (EN14387) respirator filter
分析證明 (COA)
輸入產品批次/批號來搜索 分析證明 (COA)。在產品’s標籤上找到批次和批號，寫有 ‘Lot’或‘Batch’.。
Nina Sanina et al.
FEBS letters, 587(14), 2260-2265 (2013-06-08)
The present work aimed to compare the effects of different lysophosphatidylethanolamine (LPE) content in lipids derived from Yersinia pseudotuberculosis cells exposed and not exposed to phenol on the conformation of OmpF-like porin of these bacteria. Differential scanning calorimetry and intrinsic
Amani M D Elahwany et al.
Acta biologica Hungarica, 64(1), 106-117 (2013-04-10)
Six isolates with phenol degrading ability were obtained from marine sediments by enrichment procedures and an isolate, AM4, was identified as Alcaligenes sp. by 16S rDNA sequencing. The Plackett-Burman design was applied to estimate the significance of culture medium components
Chiung-Fen Chang et al.
Water science and technology : a journal of the International Association on Water Pollution Research, 67(7), 1434-1441 (2013-04-05)
Magnetic TiO2 (MT) composites were prepared and applied to degrading phenol, which is one of the listed priority pollutants. The effects of heat treatment under preparation on the photocatalytic activity of MT composites have been investigated by varying the soaking
Z L Kiss et al.
Water science and technology : a journal of the International Association on Water Pollution Research, 67(6), 1272-1279 (2013-03-20)
After their use for heating, e.g. in greenhouses, waste thermal waters may cause environmental problems due to their high contents of ions, and in some cases organic matter (associated with an oxygen demand) or toxic compounds. The aims of this
Biju Prava Sahariah et al.
Environmental technology, 34(1-4), 245-256 (2013-03-28)
Performance of a fed batch moving-bed reactor system arranged in anaerobic (B1)-anoxic (B2)-aerobic (B3) mode was investigated using cycle time (18-36h), gradual fill time (total 5-18.5 h; B1: 1-3.7 h; B2 and B3: 2-7.4 h each) and instantaneous fill time
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