多流股换热器网络是一种新型的换热器网络。
The muhistream heat exchanger network is a new-style heat exchanger network.
包含描述一个换热器网络的稳态操作的方程序系统。
Contains a system of equations that describes the steady-state operation of a heat exchanger network.
本文对啤酒厂麦汁二级冷却的换热器网络问题进行了优化模拟。
Optimal simulation of heat exchanger networks is made for two—stage cooling of wort in beer factory.
在此基础上，重点分析和讨论了多股流换热器网络的衍生约束优化方法的具体运用。
Based on it, the concrete application of the derivation constraint optimization method of multi-flow heat exchanger network is analyzed and discussed.
计算课程10.492换热器网络的RGA（相对增益阵列）和DC（扰动成本）。
Calculates the RGA (relative gain array) and DC (disturbance cost) for the 10.492 heat exchanger network.
本文所介绍的换热器网络的通用模拟系统具有程序简单、功能全面、使用方便等优点。
A heat exchanger network simulator has been developed. It is simple in program, easy to use, and diversified in function.
为了获得最小能量需求的换热器网络，可通过窄点设计法来确定是否有必要进行物流分枝。
It is necessary to select stream splits by using pinch design method in order to obtain a minimum energy requirement network.
结果表明：应用该方法建立的换热器网络的模拟有稳定性好、能够自动处理复杂结构网络的优点。
The result shows that HEN set up using this method has the advantages of good stabilization and complicated structure HEN auto treatment ability.
基于两相流体网络，建立了针对具有复杂流路布置的翅片管换热器稳态通用分布参数仿真模型。
A general steady distributed parameters model of fin-and-tube heat exchanger with complex refrigerant circuits was developed based on two-phase fluid network.
而且此模型也可以用于求解具有不同传热膜系数和不同换热器材质的网络。
Furthermore, the model can also be used to solve heat exchanger network problems with unequal heat transfer film coefficients and different construction materials.
本文建立了由换热器、分流器和混合器构成的换热网络流程模拟系统。
This paper sets up a simulator of heat exchanger networks that consists of heat exchangers, mixers and splitters.
可用于合成换热器最佳网络。
用过程能量组合方法对某炼油厂的换热网络进行改造，新方案比原系统节能57%，并减少了两台换热器。
Heat exchanger network for one oil refinery has been improved by process energy integration technology. Energy savings of new scheme is 57%against original design and number of units decrease by 2.
用过程能量组合方法对某炼油厂的换热网络进行改造，新方案比原系统节能57%，并减少了两台换热器。
Heat exchanger network for one oil refinery has been improved by process energy integration technology. Energy savings of new scheme is 57%against original design and number of units decrease by 2.
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