代码搜索：condenser
找到约 61 项符合「condenser」的源代码
代码结果 61
www.eeworm.com/read/339293/12244605
m colamod.m
function xprime=colamod(t,X,U)
%
% colamod - This is a nonlinear model of a distillation column with
% NT-1 theoretical stages including a reboiler (stage 1) plus a
% total conden
www.eeworm.com/read/339293/12244618
m cola_db.m
function xprime=cola_db(t,X)
% sample usage: [t,x]=ode15s('cola_dv',[0 5000],0.5*ones(1,82));
%
% cola_db - Subroutine for simulation with DB-configuration.
%
%
% Inputs are distillate (
www.eeworm.com/read/339293/12244628
m cola_dv.m
function xprime=cola_dv(t,X)
% sample usage: [t,x]=ode15s('cola_dv',[0 5000],0.5*ones(1,82));
%
% cola_dv - Subroutine for simulation with DV-configuration.
%
%
% Inputs are distillate (
www.eeworm.com/read/339293/12244634
m coldmod.m
function xprime=coldmod(t,X,U)
%
% colamod - This is a nonlinear model of a distillation column with
% NT-1 theoretical stages including a reboiler (stage 1) plus a
% total conden
www.eeworm.com/read/339293/12244661
m colamod.m
function xprime=colamod(t,X,U)
%
% colamod - This is a nonlinear model of a distillation column with
% NT-1 theoretical stages including a reboiler (stage 1) plus a
% total conden
www.eeworm.com/read/339293/12244666
m colamodk2_15.m
function xprime=colamod(t,X,U)
%
% colamod - This is a nonlinear model of a distillation column with
% NT-1 theoretical stages including a reboiler (stage 1) plus a
% total conden
www.eeworm.com/read/339293/12244673
m cola_db_f1.m
function xprime=cola_db(t,X)
% sample usage: [t,x]=ode15s('cola_dv',[0 5000],0.5*ones(1,82));
%
% cola_db - Subroutine for simulation with DB-configuration.
%
%
% Inputs are distillate (
www.eeworm.com/read/339293/12244692
m cstreams.m
function [L, V] = cstreams(t,X,U)
% Inputs: t - time in [min].
% X - State, the first 41 states are compositions of light
% component A with reboiler/bottom stag
www.eeworm.com/read/339293/12244695
m cola_db.m
function xprime=cola_db(t,X)
% sample usage: [t,x]=ode15s('cola_dv',[0 5000],0.5*ones(1,82));
%
% cola_db - Subroutine for simulation with DB-configuration.
%
%
% Inputs are distillate (
www.eeworm.com/read/339293/12244697
m colamodn.m
function xprime=colamodn(t,X,U)
% NO FLOW DYNAMICS
%
% colamod - This is a nonlinear model of a distillation column with
% NT-1 theoretical stages including a reboiler (stage 1) plus a
%