林产化学与工业
林產化學與工業
림산화학여공업
CHEMISTRY AND INDUSTRY OF FOREST PRODUCTS
2015年
4期
92-96
,共5页
程毅%刘六军%李瑞
程毅%劉六軍%李瑞
정의%류륙군%리서
热异构化%驻留率%化学反应器%填充床%流体力学
熱異構化%駐留率%化學反應器%填充床%流體力學
열이구화%주류솔%화학반응기%전충상%류체역학
thermo isomerization%resident rate%chemical reactor%packed bed%fluid mechanics
在自制的冷态反应器中,以150μm铜粉为流化介质,对浅池式流化床反应器内部流体的流动特性进行了研究,并将实验测量结果与理论推导结果进行对照。结果表明:在该反应器内部填充了较大固相颗粒后,形成的流化池可以有效地延长流化时间。对流化池中驻留的流化粒子进行测量,推导出驻留率的计算公式:σ=-0.51lnu-0.4m/V+2.145。将该公式带入到Ergun方程中,得到整体床层的压降,即反应器总压降方程:Δp =150μu0d2p ×(1-ε)2ε3+74×ρu20dp ×1-εε3 Le +(1-σ)(1-εb)Leρ,得到冷态试验结果说明方程可以很好的阐述该反应器内部流体的流动特性。
在自製的冷態反應器中,以150μm銅粉為流化介質,對淺池式流化床反應器內部流體的流動特性進行瞭研究,併將實驗測量結果與理論推導結果進行對照。結果錶明:在該反應器內部填充瞭較大固相顆粒後,形成的流化池可以有效地延長流化時間。對流化池中駐留的流化粒子進行測量,推導齣駐留率的計算公式:σ=-0.51lnu-0.4m/V+2.145。將該公式帶入到Ergun方程中,得到整體床層的壓降,即反應器總壓降方程:Δp =150μu0d2p ×(1-ε)2ε3+74×ρu20dp ×1-εε3 Le +(1-σ)(1-εb)Leρ,得到冷態試驗結果說明方程可以很好的闡述該反應器內部流體的流動特性。
재자제적랭태반응기중,이150μm동분위류화개질,대천지식류화상반응기내부류체적류동특성진행료연구,병장실험측량결과여이론추도결과진행대조。결과표명:재해반응기내부전충료교대고상과립후,형성적류화지가이유효지연장류화시간。대류화지중주류적류화입자진행측량,추도출주류솔적계산공식:σ=-0.51lnu-0.4m/V+2.145。장해공식대입도Ergun방정중,득도정체상층적압강,즉반응기총압강방정:Δp =150μu0d2p ×(1-ε)2ε3+74×ρu20dp ×1-εε3 Le +(1-σ)(1-εb)Leρ,득도랭태시험결과설명방정가이흔호적천술해반응기내부류체적류동특성。
The flow equation for a novel fluidized bed reactor which contained solid particles was presented and validated by cold state experiment. The results indicated that the sump of the reactor formed by adding some relatively big particles could prolong the fluidized time effectively. Through resident rate test, its calculation was deduced as σ= -0. 51lnu-0. 4m/V+2. 145. As the pressure drop consisted of pipe flow drop and resident drop owing to the resident effect and the resident drop, the resident rate was introduced into Ergun equation and the pressure drop equation was concluded asΔp = 150μu0d2p × (1 -ε)2ε3 + 74 × ρu20dp × 1 -εε3 Le +(1-σ)(1-εb)Leρ. The experiment of cold state experiments showed that the model could match the flow state very well.