Executive Summary. Number of Low Number of High Number of Faults , Number of OK

Similar documents
Public Services Building 155 N First Avenue Hillsboro, OR March 2012

Otherwise, you can continue reading the file on the following pages.

Refrigeration System Report March 2017

SECTION 7 AIR CONDITIONING (COOLING) UNIT 40 TYPICAL OPERATING CONDITIONS

SECTION 7 AIR CONDITIONING (COOLING) UNIT 40 TYPICAL OPERATING CONDITIONS UNIT OBJECTIVES

Pressure Enthalpy Charts

Checking the Charge on a Heat Pump in the Winter

A Comparison Between Refrigerants Used In Air Conditioning

Performance of R-22, R-407C and R-410A at Constant Cooling Capacity in a 10

CHAPTER 7 PERFORMANCE ANALYSIS OF VAPOUR COMPRESSION REFRIGERATION SYSTEM IN HYBRID REFRIGERATION SYSTEM

For an administrative fee of $9.97, you can get an un-locked, printable version of this book.

Section 1: Theory of Heat Unit 3: Refrigeration and Refrigerants

R32 Compressor for Air conditioning and Refrigeration applications in China

PRESSURE-ENTHALPY CHARTS AND THEIR USE By: Dr. Ralph C. Downing E.I. du Pont de Nemours & Co., Inc. Freon Products Division

Low GWP Refrigerants for Air Conditioning Applications

AIR CONDITIONING. Carrier Corporation 2002 Cat. No

Air Conditioning Inspections for Buildings Efficiency of Air Conditioning Systems

REFRIGERATION CYCLE Principles of Mechanical Refrigeration Level 2: Cycle Analysis

SERVICE ASSISTANT OVERVIEW FDSI Online Training

Application and Installation Bulletin for Master-Bilt Refrigeration Superheat Controller Kit Assembly(A ), 120/208/240/1/60, R404A, LT/MT APPS

SECTION 2 SAFETY, TOOLS AND EQUIPMENT, SHOP PRACTICES UNIT 10 SYSTEM CHARGING

10/4/2013. The Changing State of Refrigerants

Technical Development Program

Superheat charging curves for technicians

RTP Technical Bulletin

Application Engineering

Thomas J Kelly. Fundamentals of Refrigeration. Sr. Engineering Instructor Carrier Corporation. August 20, Page number: 1.

COMPARATIVE STUDY OF NEW ECOLOGICAL GASES

Air Cooled Packaged Systems AIRAH Back to Basics

Warm Case Troubleshooting Guide 9/18/2014

Implementation and testing of a model for the calculation of equilibrium between components of a refrigeration installation

100 TON AIR-COOLED SCROLL PACKAGED. Call us today! (800) SPECIFICATIONS GENERAL DIMENSIONS ELECTRICAL DATA ADDITIONAL INFORMATION

c Dr. Md. Zahurul Haq (BUET) Refrigeration Cycles ME 6101 (2013) 2 / 25 T270 COP R = Q L

Technical Development Program. COMMERCIAL HVAC PACKAGED EQUIPMENT Split Systems PRESENTED BY: Ray Chow Sigler

Refrigeration Cycles. Refrigerators, Air-conditioners & Heat Pumps. Refrigeration Capacity/Performance. Dr. Md. Zahurul Haq

Publication # RD-0003-E Rev 1, 10/17 SERVICE GUIDELINES HCFC R22 TO HFC REFRIGERANT BLENDS

Instructors: Contact information. Don Reynolds Doug McGee Factory Tech Support

Evaporative Cooling in a Hot-Dry Climate

T270 COP R = Q L. c Dr. Md. Zahurul Haq (BUET) Refrigeration Cycles ME 6101 (2017) 2 / 23 T354

A Treatise on Liquid Subcooling

5. ASSESSMENT RECOMMENDATIONS

product application data PERFECT HUMIDITY DEHUMIDIFICATION SYSTEM

(Refer Slide Time: 00:00:40 min)

TEST REPORT #65. Compressor Calorimeter Test of Refrigerant L-41-2 (R-447A) in a R-410A Scroll Compressor

Energy Performance of Low Charge NH3 Systems in Practice. Stefan S. Jensen

Math. The latent heat of fusion for water is 144 BTU s Per Lb. The latent heat of vaporization for water is 970 Btu s per Lb.

Case 8 Basic Performance of Screw Compressor

Performance Enhancement of Refrigeration Cycle by Employing a Heat Exchanger

ENERGY SAVINGS THROUGH LIQUID PRESSURE AMPLIFICATION IN A DAIRY PLANT REFRIGERATION SYSTEM. A. Hadawey, Y. T. Ge, S. A. Tassou

THE FIVE W s SYSTEMES LMP MECHANICAL SUB-COOLING. I.G.A. GIRARD, TERREBONNE, Qc. INCREASED SYSTEM EFFICIENCY & LOWER ENERGY COSTS

EVALUATION OF REFRIGERANT R290 AS A REPLACEMENT TO R22

SECTION 5 COMMERCIAL REFRIGERATION UNIT 22 CONDENSERS UNIT OBJECTIVES UNIT OBJECTIVES 3/22/2012

MASS. MARITIME ACADEMY

To accomplish this, the refrigerant fi tis pumped throughh aclosed looped pipe system.

2016 Annual Conference

Understanding Head Pressure Control. Walter H Langille, M.A.Sc., P.Eng Sales Engineer KeepRite Refrigeration

Figure 1: Schematic of internal heat exchanger vapor-injection cycle

Technical Bulletin (TB-0037)

Virtual Refrigerant Pressure Sensors for Use in Monitoring and Fault Diagnosis of Vapor- Compression Equipment

Study Final Report. Priority Cool Refrigerant Study

NO: 9-16 DATE: 2/11/16 EMERSON CLIMATE TECHNOLOGIES WHOLESALERS -EXECUTIVES -PRODUCT MANAGERS -EMERSON TM TECHNICAL SPECIALISTS -BRANCH PERSONNEL

DAVE DEMMA ACHIEVING HEAD PRESSURE CONTROL

A/C Cooling Load calculation and measurement

HVAC/R Refrigerant Cycle Basics

Service Step by Step Trouble-Shooting Check-List

Comparative Performance of HFO Blends in a Condenser

REFRIGERANT CHANGEOVER

TEST REPORT #53. System Drop-in Test of Refrigerant Blend DR-55 in a Five-Ton R-410A Rooftop Packaged Unit

Presented By: John Dolan, P.E.

D-PAC. Digital Precise Air Control System. Functionality Factory Testing Ease of Installation Ease of Maintenance Energy Efficiency

Commercial CO2 Refrigeration Systems. Guide for Subcritical and Transcritical CO2 Applications

Air Conditioning Inspections for Buildings Efficiency of Air Conditioning Systems

Energy Use in Refrigeration Systems

HVAC Water chiller selection and optimisation of operation

MYSTICOOL Max Valve System with Xstream and A.R.M.E.D. Technology Service & Installation Instructions Page 1

BASIC HEAT PUMP THEORY By: Lloyd A. Mullen By: Lloyd G. Williams Service Department, York Division, Borg-Warner Corporation

Evaporative-Cooled vs. Air-Cooled Chillers: Kirtland AFB Case Study

DIRA S.L. (Desenvolupament, Investigació i Recerca Aplicada S.L.)

500 EX Fusion Compressor Series

Analysis of Constant Pressure and Constant Area Mixing Ejector Expansion Refrigeration System using R-1270 as Refrigerant

XSTREAM Valve System With A.R.M.E.D. Technology Service & Installation Instructions Page 1

3. (a) Explain the working of a rotary screw compressor. [10] (b) How the capacity control is achieved in refrigerant compressor?

Packaged Heat Pump. 20 Ton Rooftop Units with ReliaTel TM Controls NOTICE

Refrigerant changeover guidelines

Pack Calculation Pro. Users guide. Version Morten Juel Skovrup

Applications of Thermodynamics: Heat Pumps and Refrigerators

Numerical Study on Improvement of COP of Vapour Compression Refrigeration System

The Refrigeration Cycle. Jerry Cohen President Jacco & Assoc.

Case 15 Refrigeration System for Chemical Fertilizer Plant Ammonia Storage

Transcritical CO2 Bottle Cooler Development

CO2 TRANSCRITICAL BOOSTER SYSTEMS

TEST REPORT #14. System Drop-In Test of Refrigerant Blend ARM-42a in an Air-Cooled Screw Chiller

USING THE P-T CARD AS A SERVICE TOOL

Performance of an Improved Household Refrigerator/Freezer

Study of R161 Refrigerant for Residential Airconditioning

Workshop on AFDD for RTUs Moving from R&D to Commercialization July 13, Introduction

An Experiment of Heat Exchanger Produces Hot Water Using Waste Heat Recovery from Air Conditioning

Small Commercial Business Energy Audits. Recognizing and addressing the special requirements of the small business market segment.

Performance Enhancement of Refrigeration Cycle by Employing a Heat Exchanger

Carwin COMPRESSOR SELECTION PROGRAM

Transcription:

Unit Lower limit Upper limit Air on Model no evap. F Air off evap. F dt air evap. F Executive Summary Evapo. F This is a summary chart for quick reference and view of all the systems tested. Red boxes indicate measured levels that were out of range. There were faults in evaporator dt, condenser dt, superheat, subcool, and isentropic efficiency of the compressors. Fault levels are determined from manufacturer s recommendations and testing experience. EER at Ambient Temperatures 32.0 10.0 21.0 15.0 67 40.0 15.0 24.0 20.0 78 dt air- Super Air on Air off dt air Conde dt air- Sub cool Comp evap heat cond. F cond. F cond. F n. F cond F eff. AH 10 C1 Model# 50HJQ016--- 71.3 56.6 14.7 38.2 33.1 14.6 84.4 107.9 23.5 120.3 35.9 31.3 71.4 13.2 7.4 8.1 AH 10 C2 Model# 50HJQ016--- 71.3 56.6 14.7 39.1 32.2 24.2 84.4 107.9 23.5 121.4 37.0 34.2 69.7 12.9 7.4 7.9 GE 2 Model#48TJE004--- 71.9 56.7 15.2 39.5 32.4 23.4 80.3 95.5 15.2 115.0 34.7 19.0 68.8 13.3 3.0 3.3 GE 3 Model# 48TJE005--- 75.5 58.6 15.6 35.9 39.6 27.7 81.0 95.2 14.2 120.0 39.0 26.9 62.4 10.9 4.3 3.9 GE 7 Model# 48TJD007---621-- 72.1 48.7 23.5 31.1 41.0 33.3 81.1 106.0 24.9 112.0 30.9 18.4 73 12.8 5.8 6.2 GE 8 Model# 48TJD008--- 79.5 59.4 20.1 37.9 41.6 28.1 81.3 94.7 13.4 120.0 38.7 17.8 64.1 11.1 4.3 4.0 GE 13 Model# 48TJD007---621-- 76.2 47.5 28.7 36.0 40.2 18.7 76.6 98.8 22.2 111.0 34.4 20.1 74.5 14.5 5.4 6.5 GE 15 C1 Model# 48TJD008--- 69.1 51.9 17.2 37.1 32.0 21.3 73.7 90.7 17.0 113.5 39.8 16.8 68.5 12.9 3.4 3.7 GE 15 C2 Model# 48TJD008--- 69.1 51.9 17.2 43.2 25.9 0.0 73.7 90.7 17.0 132.0 58.3 23.6 71.2 12.6 3.9 4.1 Mean 18.5 35.3 21.3 19.0 38.7 23.1 69.3 12.7 Max 79.5 59.4 28.7 41.6 33.3 84.4 107.9 24.9 58.3 34.2 74.5 14.5 Min 69.1 47.5 14.7 25.9 0.0 73.7 90.7 13.4 30.9 16.8 62.4 10.9 Number of Low 1.0 0.0 Number of High 7.0 5.0 Number of Faults 3.0 8.0, 9.0 5.0 2.0 Number of OK 6.0 1.0 0.0 4.0 7.0 EER Power kw Cooling cap Note: these are measured EER, not equipment rating. This graph shows the EER each circuit was operating at during the test at the average ambient. It would be expected to see a drop in EER the further to the right the units get, as EER should drop as ambient temperature rises.

EER and Return Air Temperature Note: these are measured EER, not equipment rating. This graph shows the EER of each circuit during the test with the Return air to the evaporator. You would expect to see a drop in EER the further right each unit gets, as the higher the return air temperature gets the lower the EER should be. 2 P a g e

Measured EER Results 20 15 10 5 0 AH-10 C1 AH-10 C2 GE-2 GE-3 GE-7 GE-8 GE-13 GE-15 C1 GE-15 C2 ClimaCheck Measured EER Nominal EER for the compressor at measured conditions (Copeland Compressor design EER) Expected Nominal EER This Graph shows three different EER metrics. ClimaCheck takes multiple measurements then uses thermodynamic calculations to get the EER level. A Copeland software program was used to calculate design EER levels for the compressor. A compressor in Copeland s software was chosen that was closest in comparison to the compressor on the Carrier unit, but as it is not identical, the data will vary somewhat. Measurements that the ClimaCheck took were imported into the software to get the nominal EER level. This is essentially the EER that the compressor should be running in these conditions. The expected EER was derived from the software by averaging data from multiple conventional RTUs with no known problems that were tested previously with the ClimaCheck. This is not a perfect calculation, but a reasonable expectation of unit performance if there are no problems. Below are the averages used for Expected Nominal EER. Evaporation Temperature = evaporator entering air -35 F (the average delta T entering air to evaporation temperature on previous units tested without issues) Condensing Temperature = ambient Temperature + 25 F (the average delta T entering air to condensing temperature on previous units tested without issues) Superheat = Average temperature of 10 F Subcool = Average temperature of 15 F 3 P a g e

Compressor Isentropic Efficiency Compressor isentropic efficiency is a comparison of the actual compression process efficiency vs. the theoretical efficiency of a perfect compression process. This compressor is averaging about 63% isentropic efficiency. Most of the other compressors in this test were around 70%. This unit and GE-3 are the only two units tested that have Tecumseh compressors. It is interesting to see that these two units also have the lowest EER of all units tested. The difference between 63% and 70% is only 7% but the difference in performance is actually 11%. 4 P a g e

GE-15 GE-15 conditions a large break room with refrigerated vending machines in it that produce a constant load. This unit conditions with 2-stage mechanical cooling and natural gas heat. Refrigeration Process Discharge Temp Circuit 1 Discharge Temp Circuit 2 Superheat Circuit 1 Superheat Circuit 2 This unit has two stages of cooling using the same evaporator and condenser coils though the refrigeration circuits are separate. Both refrigeration circuits are almost identical and should run almost identical. However, this graph shows that this is not the case during this test. Circuit 2 has 0 superheat. Superheat this low brings the discharge temperature down. 5 P a g e

Superheat Superheat Circuit 1 Avg. 22 F Superheat Circuit 2 Avg. 0 F Most RTUs are efficient between 10-15 F of superheat and many manufacturers suggest this range. However, with Carrier s Acutrol fixed orifice metering device the refrigerant charge is the greatest determining factor of the superheat level. As outside ambient temperatures and indoor space temperatures change this affects the superheat and causes it to change as well. Circuit 1 is averaging about 22 F of superheat. The charging chart on page 59, shows the superheat should be at about 9 F (±5 suction temp) in these conditions. Circuit 2 rapidly drops to 0 of superheat as the test starts. The charging chart on page 58 shows this circuit should be operating at about 11 F of superheat (±5 suction temp). 6 P a g e

Subcool Subcool Circuit 2 Avg. 25 F Subcool Circuit 1 Avg. 17 F Both refrigeration circuits should have the same refrigerant charge in them. If the circuits have the same charge and are operating the same you would see the subcool of both circuits at the same level. It would be expected that with the very low superheat of circuit 2, it would have a lower subcool as well because too much refrigerant is in the evaporator and not the condenser. That is not the case. Circuit 2 has high subcool that may be causing the low superheat. Similar units to this one would run around 15-20 F subcool in these conditions, however, all of the units on this roof have issues with condenser coil corrosion. It is difficult to measure the level of corrosion so it is very difficult to say where the subcool should be with a corroded condenser coil. If the refrigerant charge is correct it would be expected that the worse the corrosion is the higher the subcool would be. Although evaporator air inlet temperature would have to be taken into account as well. 7 P a g e

Condenser Condensing Temperature circuit 2 Condensing Temperature circuit 1 Avg. DT of 40 F Avg. DT of 55-60 F Air inlet temperature at Condenser The blue and green at the top of the graph shows the condensing temperature of circuits 1 and 2. At the bottom of the graph, (in light blue) is the air temperature at the inlet of the condenser. The difference of these would be referred to as the delta T air inlet to condensing temperature. During the test the delta T air inlet to condensing averaged close to 40 F on circuit 1 and 55-60 F on circuit 2. A new higher efficiency RTU with good controls could run 10-15 F dt. Older units are usually around 20 to 25 F dt. This higher dt level than usually seen on DX air conditioners and may indicate a problem with the condenser s ability to transfer heat. The 60 F dt of circuit 2 is indicating a major problem. 8 P a g e

Evaporator Evaporation Temperature Circuit 2 Evaporation Temperature Circuit 1 The high pressure side of the system and the low pressure side of the system are only separated by the fixed orifice metering device (Carrier Acutrol) on this system. If the high pressure increases, there will be more gas forced through the metering device at a higher pressure causing the low pressure side of the system to rise in pressure as well. On the condenser graph on previous page circuit 2 is operating at a higher condensing temperature than circuit 1. This higher temperature comes from a higher pressure. The evaporator shows evidence of this as well circuit 2 has a higher evaporation temperature than circuit 1. This higher evaporation temperature comes from a higher suction pressure that is caused by a higher condensing pressure. The saturated suction pressure of circuit 2 is higher than circuit 1 because the condensing temperature and pressure of circuit 2 are very high. 9 P a g e

Charging Chart GE-15 Circuit 1 and 2 Suction line temperature = 46 R-22 refrigerant at 65# psig =37 46-37 = 9 super Suction line temperature = 54 R-22 refrigerant at 73# psig =43 54-43 = 11 superheat This is a Carrier Charging Chart. All Carrier units have this sticker mounted on them to help a technician make sure there is a correct refrigerant charge. The red is plotted on the chart from test data. The green represents where the plot should be. Circuit 1 chart shows refrigerant should be added to the circuit. Circuit 2 shows that refrigerant should be removed from the circuit. They also indicate that the superheat on circuit 1 should be 9 F and circuit 2 should be 11 F at these temperatures and pressures. It is not recommended that the unit run at this superheat. If refrigerant were to be added and removed the pressures and temperatures will change causing the superheat to change. 10 P a g e

Conclusion Superheat The superheat of circuit 1 is dangerously low and will be causing lubrication issues in this compressor every time it runs. These lubrication issues will damage the compressor and shorten its life expectancy. Condenser The difference between condenser air inlet temperature and condensing temperature are very high. This would indicate poor heat transfer at the condenser coil between the air and the refrigerant on circuit 1. However, Circuit 2 is much worse and both circuits are using the same condenser. There were no visual conditions of the condenser to suggest either circuit would get more or less air flow or heat transfer than the other. Summary The condenser coil is where heat is removed from the conditioned space and released into the ambient conditions. The better the heat transfer is at the coil the more efficient the unit is. As the heat transfer drops at the coil the unit becomes less efficient. GE-15 had 69 F air onto the evaporator and 74 F air onto the condenser with 113 F and 132 F condensing temperatures. This was a low load situation and the unit should not have produced condensing temperatures this high under these conditions. With these problems this unit would be extremely inefficient at higher load conditions and may cause damage or compressor failure. It is evident this condenser coil has serious problems transferring heat. Efficiency would be increased if this condenser coil was replaced. Circuit 2 seems to have more problems than just poor heat transfer between the refrigerant and the air at the condenser coil. The manufacturers charging chart suggests removing refrigerant from this circuit. It is a good recommendation, but with a condensing temperature this high, it would be expected that the subcooling would be much higher than it is. It is possible for non-condensables in the refrigerant circuit to cause this. The ClimaCheck is a great tool for detecting non-condensables, such as air or nitrogen in a refrigeration circuit, even in very small amounts. Typically, the isentropic efficiency would rise to a fictitious range and conversions such as superheat and subcool could show impossible negative readings. The superheat dropped to 0 F, which is the lowest level possible and stayed right there without going below 0 F. The isentropic efficiency was in an expected range. This is a good indication there are not any non-condensables in the system. The compressor of circuit 2 is in danger of failure running the way it is now. It would be much more cost effective to take action now than wait for it to fail, costing the owner replacement cost, down time, and occupant discomfort. Even with all of the problems circuit 2 has shown, it is only running about 2.5% less efficient than circuit 1. Circuit 1 averaged a 12.9 EER and Circuit 2 averaged a 12.6 EER. Both of these EER levels should be higher in these conditions. The issue with the condenser is the reason for the lower than expected EER levels. The ClimaCheck only measures the actual performance of the unit in real time at the conditions during the test. It is hard to estimate what the unit should run at under different conditions or with no problems opposed to problems. On the next page, there are illustrations to help show performance at different conditions. The three illustrations below show the compressor data for the compressors in GE-15. This is nominal data supplied by Copeland software, the manufacturer of the compressors in GE-15. The top illustration shows the temperatures and pressures of circuit 1 and the expected performance of the compressor with a 12.42 EER. The second illustration shows the expected performance at these conditions with a 14.93 EER. If this unit was operating at this EER, it would be a 20% increase in performance at these conditions. The second chart shows the temperatures and pressures circuit 2 running at and the expected performance of the compressor with a 10.43 EER. The bottom chart shows temperatures and pressures that would be expected of this unit under these conditions, if there were no issues. It shows an EER of 14.93, this is a 43% increase in performance at these conditions. 11 P a g e

Example: nominal running performance at these conditions Circuit 1 Example: nominal running performance at these conditions Circuit 2 12 P a g e

Example: expected nominal performance at these conditions Circuits 1 and 2 13 P a g e