introduction of room air conditioner system simulation ...€¦ · multi-unit ac system has more...

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1 Prof. Guoliang Ding Haoran Sun Institute of Refrigeration and Cryogenics Shanghai Jiao Tong University 2014-10-17 Introduction of Room Air Conditioner System Simulation Platform

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Page 1: Introduction of Room Air Conditioner System Simulation ...€¦ · Multi-Unit AC system has more input and output parameters, which means the GUI need to be redesigned. Multi-Unit

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Prof. Guoliang Ding Haoran Sun

Institute of Refrigeration and Cryogenics

Shanghai Jiao Tong University 2014-10-17

Introduction of Room Air Conditioner System

Simulation Platform

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Content

I. Function and Architecture of the Software

II. Mathematical Model and Algorithm

III. Graphic User Interface of the Software

IV. Example for 2600W AC system

V. Proposal for Next Step

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Function of the software

Refrigerant:

AC System simulation Platform

Unit Setting: SI English

System Type: Cooling Only Cooling & Heating

R410A R22

R290 R32

Compressor Data Import

Confidential Data Protection

Performance Simulation

Analysis for performance parameters

Operating Systems: Win 7 & Win 8 Chinese & English

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Architecture of the software

The software is able to employ user’s compressor data in the simulation process, and the data can be imported as a DLL file.

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Content

I. Function and Architecture of the Software

II. Mathematical Model and Algorithm

III. Graphic User Interface of the Software

IV. Example for 2600W AC system

V. Proposal for Next Step

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Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

1) General model can not reflect the compressor specific performance

2) Ten coefficient model doesn’t fit for the system simulation progress

3) The confidential data of the compressor can not be easily obtained

Existing Problems

1) Using product data to reflect the compressor characteristics

2) Having wide application range to fit system simulation progress

3) Protect product confidential data

Solution — Developing a Product Data Interactive Model

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— Technical Roadmap

Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

Mass Flow Rate Correlation

Compressor DLL File

Mass Flow Rate Fitting Data

Mass Flow Rate linear Model

Simulation Package

Shown in the GUI

From DLL

Fitting

Ref-Oil Solubility

Correlation

Input Power Correlation

Ref-Oil Solubility Correlation

Product Informations

Input Power Fitting Data

Input Power linear Model

From DLL

FittingProduct

Informations

Product Data

Black Box Encapsulation

Using in the Software

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— Mass Flow Rate Equation

基于理论的变频压缩机线性化流量模型:

0 1 2 3o o

x x xi i i

p pVm C C f C C fv p p

= + + +

o

i i

pVm f a bv p

= +

引入质量流量理论模型

变频压缩机质量流量产品数据(20系数模型)20

3

10 0, 3i j i j

n e c rn

m c T T f i j i j− −

=

= ≥ ≥ + ≤∑ , ,其中

将频率项线性化

其中 1 2( ), ( )a F f b F f= =

将系数线性化

Accuracy Validation

Application Range

- Maximum Error:5.9%

- Average Error:2.6%

Applicable in large range (Te: from -30 oC to 30 oC)

Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

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— Input Power Equation Accuracy Validation

Application Range

- Maximum Error:4.1%

- Average Error:1.6%

Applicable in large range (Te: from -30 oC to 30 oC)

Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

代入整理得:

代入整理得:

功率计算理论模型:

变频压缩机功率产品数据:

其中

计算出的功率记为{yk}n

选取 3 n 组工况,记为{x1k}n、{x2k}n,其中k=1、2、3,n≥2。

采用求解残差极小值法实现线性拟合

引入残差

拟合得到模型系数a、b、c

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const4

2 == GDm π

const=hLvG

DfvGP d

21dd 22 +=−

Basic Equation

The continuity equation:

The energy equation:

The momentum equation:

Adiabatic capillary

Superheated

Two-phase

Subcool

Superheated refrigerant in the capillary

( ) ( )sh2

1sh

2sh2

2sh2sh1sh1sh

22sh

21sh

sh ln2 fGppG

vpvpppDL

+

+−

=

[ ]

−+−

−−−

−+= *

2tp111

1*tp2

12*

2tp11

*2tp*

tp )1(ln1

1)1(

1)1(

ln pkkk

kpkkpkk

pL

vGfdpL 2

sc

scsc

2∆=

Two-phase refrigerant in the capillary

Subcooled refrigerant in the capillary

Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

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Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

( )wallriroutr,inr,r TTAHHQ −⋅⋅=−= α Refrigerant side:

Air side: ( )wallaooaouta,ina,a TTAHHQ −⋅⋅=−= ηα

total f accp p p∆ = ∆ + ∆

Energy equation: =r aQ Q

`

Subcooling Two-phase

Air

Ref

`

Two-phase Superheat

Air

Ref

Condenser

Evaporator

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Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

Indoor Unit • Cooling Mode: Down-flow Evaporator • Heating Mode: Reverse-flow Condenser

Outdoor Unit • Cooling Mode: Cross-flow Condenser • Heating Mode: Cross-flow Evaporator

Outdoor Unit has subcooling tubes, which makes refrigerant split at different point in different operation modes.

Problems

Refrigerant flow direction changes when operation mode switches

Developed model considering multi-path flow circuitries and multi-operation modes

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Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

— Existing System Simulation Algorithm

I. High demands for capillary and compressor matching, while engineers may input random parameters which will result in calculation divergence

II. The refrigerant in the evaporator outlet must be superheated, while NOT all the AC systems meet this requirement

III. Three coupled iteration loops result in SLOW computing speed

Shortcomings of Existing Algorithm

Developing new algorithm is necessary

开始

假定

压缩机计算

冷凝器计算

毛细管计算

蒸发器计算

为假定值?

计算充注量为输入值?

结束

输出结果

调整

调整

调整

Loop3

Loop2

Loop1

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Mathematical model and Algorithm Compressor Capillary Heat Exchanger System

— Developed System Simulation Algorithm

Condenser model

Evaporator model

End

N

N

Y

Y

N

Start

Capillary model

Adjust Pe

Adjust Pc

Assume Mcom, Meva, Mcon, Pe, Pc

Output Results

Loop1

Loop2

Meva (+Mcom)converge?

Adjust Mcon, Meva,

Mcom

Compressor model (Calculate ref mass)

High backpressure compressor

Low backpressure compressor

Compressor model (Calculate ref mass)

Mcon (+Mcom)converge?

Loop1

YN

YN

Compressor model(Calculate mass flow rate)

Y

Mass-induced Iteration Adjusting refrigerant mass in each component

instead of Tc to balance mass flow rate avoids the possibility of calculation divergence result from capillary and compressor matching

Adopting refrigerant mass as convergent criterion instead of superheat degree avoids the possibility of calculation divergence result from system performance

Parallel calculation loop Using two parallel calculation loops instead of

coupled loops increases computing speed

Key Technique

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Content

I. Function and Architecture of the Software

II. Mathematical Model and Algorithm

III. Graphic User Interface of the Software

IV. Example for 2600W AC system

V. Proposal for Next Step

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Main menu and toolbar

Status bar

Main Interface Compressor Heat Exchanger System Data Results

Graphic User Interface of the Software

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Graphic User Interface of the Software Main Interface Compressor Heat Exchanger System Data Results

Import product DLL

Choose DLL file

Import successfully

Show product public information

To protect user’s confidential data, the compressor data is imported as a DLL file. Only public information is shown in the interface.

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Graphic User Interface of the Software Main Interface Compressor Heat Exchanger System Data Results

The compressor DLL file is built through the program template and checked by the test tool provided by SJTU

Program Template Compressor DLL Test Tool

Import DLL Basic Information

Working Condition

Single Point Multi-Points

User Defined Functions

Rebuild all

Compressor DLL File

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Graphic User Interface of the Software Main Interface Compressor Heat Exchanger System Data Results

Indoor Unit

Tubes

Smooth / Enhanced

Fins

Wavy / Slit / Super Slit / Louver / Plate

Block Type

Inlet Air Status

Block Structures

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Graphic User Interface of the Software Main Interface Compressor Heat Exchanger System Data Results

Outdoor Unit

Tubes

Smooth / Enhanced

Fins

Wavy / Slit / Super Slit / Louver / Plate

Block Type

Inlet Air Status

Block Structures

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Graphic User Interface of the Software Main Interface Compressor Heat Exchanger System Data Results

System Settings

Capillary Connection Line

Unit Selection

Operation Mode: Cooling / Heating Ref Type: R22/R290/R32/R410A

SI English

Main Tube Sub Tube Connection Line

Suction Line

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Graphic User Interface of the Software Main Interface Compressor Heat Exchanger System Data Results

Details

Cooling Capacity EER Condensing Temp. Evaporating Temp. … Indoor Unit / Outdoor Unit:

Air Outlet Dry Bulb Temp. Air Outlet Wet Bulb Temp. Heat Transfer Coefficient …

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Content

I. Function and Architecture of the Software

II. Mathematical Model and Algorithm

III. Graphic User Interface of the Software

IV. Example for 2600W AC system

V. Proposal for Next Step

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Example for 2600W AC system

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Content

I. Function and Architecture of the Software

II. Mathematical Model and Algorithm

III. Graphic User Interface of the Software

IV. Example for 2600W AC system

V. Proposal for Next Step

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Proposal for Next Step

Development of Multi-Unit AC System Simulation Software I. Multi-Unit Air Conditioners have been widely used.

II. The use of small diameter copper tube is an effective way to reduce volume of heat exchanger, cost and refrigerant charge.

III. Employing small diameter copper tube in multi-unit AC system is challenged because of much more complex refrigerant distributions and system matching.

IV. Control algorithm of multi-unit system is hard to optimize experimentally.

V. A simulation software to predict system performance is needed.

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Proposal for Next Step

Technique Requirement

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Proposal for Next Step

What need to do I. Extend Single Unit System Algorithm to Multi-Unit System

II. Develop method to adopt user’s control algorithm

III. Develop control method for Part-Load Working Condition

IV. Develop GUI for Multi-Unit System

Multi-Unit AC system has several indoor units, which means more unknown variables in the simulation process, making system simulation algorithm more complex.

Multi-Unit AC system has variable control algorithms, which means it is difficult to find a general way to import user’s variable control algorithm and to use in the simulation process.

Multi-Unit AC system has more input and output parameters, which means the GUI need to be redesigned.

Multi-Unit AC system has more adjustable parameters than single unit system, which makes the control method for part-load working condition is more complex.

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The End

Thank you!