Midco HMA-2A Service Manual

Installation and Service Instructions
MADE in the USA
HMA 2 & HMA 2A
Direct-Fired Gas Burners
The Blue Flame Series
DIRECT FIRED MAKE-UP AIR BURNERS are used in industrial and commercial applications to maintain the desired environmental temperatures required by critical processes i.e. health purposes, production systems, quality control, comfort and loss prevention where it is necessary or required to exhaust large amounts of conditioned air.
Make-up Air Systems used as stand alone heating systems or operating in combination with central heating plants systems can be cost effective in three ways: 1) reducing the initial expenditures, 2) tempering incoming air which may extend the life of expensive central heating plants and 3) reducing excessive equipment cycling or premature component failures due to increased heating demands.
Our innovative two stage combustion burner is not just a modifi cation or improvement of the old, but a completely new approach to direct-fi red combustion. The two-stage combustion improves control of the fl ame process, meets or exceeds the new ANSI Standards while outperforming the competition. By incorporating two separate fl ames within the burner combustion zone, the fl ame is more stable, shorter and cleaner, permitting the reduction of emissions levels and allowing for higher temperature rise and higher tolerance to varying conditions when placed in the profi le opening.
Features and Benefi ts
Reduced NO2 and CO Emissions: Lower emissions levels that pass the ANSI Z83.4, Z83.18 and Z83.25 standards.
Higher Temperature Rise: The two stage combustion process lowers NO temperature rise.
Increased Capacity: Up to 750,000 BTU’S per foot. (Higher BTU levels can be achieved if ANSI Z83 Standards for CO and NO
emissions are not of a concern. Process heaters can fi re
2
up to 1,000,000 BTU’S a foot or more.)
Increased Differential Pressure Drop and Higher Velocities: HMA 2 & 2A burners can operate as low as 0.05″ to 1.4″ W.C. differential pressure range or in air velocity as low as 800 fpm to 4000 fpm.
Flame Stability: Two stage combustion provides better fl ame stability and emission control, allowing for a shorter fl ame and easier profi le confi guration.
Reduced Inventory Costs - HMA 2A: Single burner casting can be fi red with natural, propane or butane gas burner inventory.
Reduced Shipping Costs: A smaller, lighter casting than the competition’s, can lower your freight costs.
Turndown: 30-1 turndown can be achieved with proper modulating controls and valves. (Higher turndown possible depending on equipment design.)
emissions which is the limiting factor in
2
1
, reducing
Midco® International Inc. 4140 West Victoria Street Chicago, Illinois 60646 toll free 866.705.0514 tel 773.604.8700 fax 773.604.4070 web www.midcointernational.com e-mail sales@midcointernational.com
Emission performance is application specifi c and may vary.
1
Consult Midco for applications using butane fuels.
Quality Designed for Proven Performance
1113
8471 34
Printed in USA
Specifi cations
Specifi cations
*Firing Rate .............................................................. Up to 750,000 Btu/hr/ft
750,000+ Contact Midco Burner Manifold Pressure
Natural Gas ................................................. 4.2 to 8 inch W.C.
Propane Gas .............................................. 1.6 to 3 inch W.C.
Pilot Capacity ............................................................ 12,000 Btu/hr
Pilot Manifold Gas Pressure
Natural Gas ................................................. 3.5 inch W.C.
Propane Gas .............................................. 2.0 inch W.C. **
Pressure Drop Across the Burner ............................ 0.05 to 1.4 inch W.C.
Air Velocity Across the Burner ................................... 800 to 4,000 FPM
Burner Turn-down Ratio ........................................... 30 to 1 (based on Btu / ft)
Flame Length ....................See page 5 for fl ame length Chart 5, and Tables 2 & 3
* Firing rate is dependent on the pressure across the burner. Please see the included charts for recommended burner sizing.
** Using a natural gas pilot on propane.
Cast Iron (CI) Aluminum (AL)
*** Burner Confi gurations HMA 2 HMA 2A HMA 2 HMA 2A
2″ Straight Section (2A only) - - - 1020810
6″ Straight Section 1050700 1050710 1050800 1050810
6″ Straight Section with Back Inlet 1230700 1230710 1230800 1230810
12″ Straight Section 1010700 1010710 1010800 1010810
12″ Straight Section with Back Inlet 1060700 1060710 1060800 1060810
Elbow Section 1070700 1070710 1070800 1070810
Tee Section 1080700 1080710 1080800 1080810
**** Pilot Confi gurations Part # Natural # Propane #
Brute Pilot Spark Rod and Flame Rod 1190850 1190950
Brute Pilot Spark Rod and UV Mount 1200350 1200450
Brute Pilot Spark Rod 1342-03
Brute Pilot Flame Rod 1360-03
(Direct) Spark Rod and Flame Rod 1190800 1190900
(Direct) Spark Rod and UV Scanner Mount 1200300 1200400
Remote Flame Rod 1220800
Remote UV 1240800
Pilot with Spark Rod only 1210800 1210900
Flame Rod
Spark Rod (Direct Spark) 1342-06
*** See Page 14, Figure 6 for burner confi guration reference.
**** See Page 15, Figure 7 for pilot confi guration reference
(Direct Spark, Std + Brute)1360-03
Table 1 - Burner and Pilot Con gurations
Midco International Inc. reserves the right to change the construction or confi guration of its products at any time. All information is based on laboratory testing. Different unit size and/or confi gurations may affect data.
2
Midco International Inc.
8471 34
HMA 2 & HMA 2A Burner Performance
Burner Performance
5.0
4.0
CO Emission
3.0
2.0
CO (PPM)
1.0
0.0 0
20
40 60 80 100 120
Temperature Rise*
750,000 Btu/hr/ft at 1.1" W.C. pressure drop across the burner
5.0
4.0
CO Emission
3.0
2.0
CO (PPM)
1.0
0.0
0 20406080100
Temperature Rise*
550,000 Btu/hr/ft at 0.6" W.C. pressure drop across the burner
5.0
4.0
120
0.5
NO Emission
2
0 20406080100120
0.4
0.3
0.2
0.1
0.0
Temperature Rise*
750,000 Btu/hr/ft at 1.1" W.C. pressure drop across the burner
0.5
NO Emission
2
0 20406080100120
0.4
0.3
0.2
0.1
0.0
Temperature Rise*
550,000 Btu/hr/ft at 0.6" W.C. pressure drop across the burner
0.5
NO Emission
2
0.4
2
NO (PPM)
2
NO (PPM)
3.0
2.0
CO (PPM)
1.0
0.0 0 20406080100
CO Emission
120
Temperature Rise*
350,000 Btu/hr/ft at 0.35" W.C. pressure drop across the burner
100
90
80
2
70
60
50
40
30
x
20
NO (PPM at 3% O )
10
0.0 0
NO Emissions Profile
x
100000 200000 300000 400000 500000 600000
Heat Input (Btu/hr/ft)
0.3
0.2
0.1
0
20
40 60 80 100 120
0.0
Temperature Rise*
350,000 Btu/hr/ft at 0.35" W.C. pressure drop across the burner
.45 Delta P
.64 Delta P
.85 Delta P
* For higher temperature rise contact Midco Engineering Department.
NOTE: Emission performance is application specific and will vary
2
NO (PPM)
8471 34
Chart 1 - CO and NO2 Emissions Data
Midco International Inc.
3
HMA 2 & HMA 2A Burner Performance
Burner Performance Continued
800,000
700,000
600,000
BTU/hr/ft
500,000
400,000
300,000
9.0
8.0
7.0
6.0
5.0
4.0
(Manifold)
3.0
Natural Gas
Propane Gas
0.20 0.40 0.60 0.80 1.00 1.20
Pressure Drop across the Burner ("W.C.)
Chart 2- BTU’s verses Pressure Drop
Natural Gas
2.0
Fuel Gas Pressure ("W.C.)
1.0
0.0 100,000 200,000 300,000 400,000 500,000 600,000 700,000
Propane Gas
BTU/hr/ft
Chart 3- BTU’s verses Gas Pressure ( W.C.)
4,500
4,000
3,500
3,000
2,500
2,000
Profile Velocity (SFPM)
1,500
1,000
0.20 0.40 0.60 0.80 1.00 1.20
Pressure Across the Burner ("W.C.)
Chart 4 - Pressure Across the Burner verses Pro le Velocity
___________________________________
4
Midco International Inc.
8471 34
Installation
- Velocity and pressure drop fi gures shown in Table 2 apply to standard design conditions. However, these conditions apply only when air enters the heater at 70° and requires little or no heat. In practice with the burner operating, these fi gures will vary, especially with inlet air at the minimum design temperature. This is because the blower handles a constant volume of air regardless of its temperature. When the air is heated expansion takes place ahead of the blower and just downstream of the burner. It follows therefore that when the air is being heated a lesser volume enters the heater, causing a reduction, both in velocity and pressure drop at the burner. Table 2 shows the variation for minimum temperature air entry and with full input to the burner. Flame lengths given in Table 2 and Chart 5 apply to conditions shown in Table 2.
Air fl ow at burner Approximate length of fl ame based on 70° (std) Burner Capacity (per foot) projecting beyond end of blower rating Natural & Propane Gas burner and profi le plate * Design Design Pressure Max. Min. velocity drop capacity capacity Turn 550,000 650,000 750,000 FPM ″ W.C Btu/Hr Btu/Hr Down per ft per ft per ft 3200 .7″ 550,000 19,000 29:1 13″ 16″ 20″ 2850 (ideal) 2500 .45″ 550,000 17,000 32:1 17″ 20″ 24″
Reduce capacity 4% per each 1000 ft altitude over 2000 ft.
.55″ 550,000 18,000 30:1 15″ 19″ 22″
Table 2 - Design Data for Pull-Thru System
* Flame lengths are given to the end of the main mass of fl ame, excluding any isolated wisps or fl ashes, and for normal operations ie. with cold inlet air (design minimum)
Air Flow Variations Due to Heating in a
Pull-Thru System
Velocity Pressure Air Actual cold Actual cold at burner drop at temp. air velocity air pressure
(from Table 1) burner rise at burner drop at burner
3200 fpm .7″ W.C.
100° 2600 fpm .46″ W.C.
2850 fpm .55″ W.C.
100° 2300 fpm .36″ W.C.
2500 fpm .45″ W.C.
100° 2000 fpm .29″ W.C.
75° 2750 fpm .52″ W.C.
75° 2450 fpm .41″ W.C.
75° 2150 fpm .33″ W.C.
Table 3 - Air Flow Variations for Pull-Thru System
EXAMPLE: A heater rated for 100° rise, 70° outlet temperature at a design velocity of 2850 fpm and a design pressure drop of .55″ W.C., will in actual operation pass 2300 fpm over the burner with a .36″ W.C. drop when air enters at -30°.
HMA 2 & HMA 2A Flame Length
35
30
750,000 Btu/ft
650,000 Btu/ft
25
550,000 Btu/ft
20
15
10
Flame Length ( inches )
5
0
1.20.2 0.4 0.6 0.8 10
Pressure Drop ( " W.C.)
Chart 5 - HMA 2 & 2A Flame Length
HMA 2 & HMA 2A fl ame length as a function of pressure drop and fi ring rate applies to push and pull through systems using 100% fresh standard air.
8471 34
Midco International Inc.
5
Installation
Profi le Setup
1. Required BTU: BTU/hr = Blower SCFM x Desired Temp. Rise x 1.08 / .92
2. Required Burner Length: Feet of burner = [Required BTU/hr]÷[Burner Firing Rate (BTU/hr/ft)] The Burner Firing Rate should correspond to the pressure drop across the burner shown in Chart 2.
3. Required Profi le Area: Total Burner Area = Number of burner sections x burner area
(Burner Section) Burner Area 2 inch 0.11 sq. ft. 6 inch 0.32 sq. ft. 12 inch 0.65 sq. ft. T Section 0.77 sq. ft. Ell Section 0.65 sq. ft.
Net Profi le Area = Rated Fan (SCFM) ÷ Profi le Velocity (SFPM) The Profi le Velocity can be determined from the following:
Profile Velocity
P is the pressure drop across the burner
Profi le Area = Net Profi le Area + Total Burner Area ___________________________________
=
945
PΔ
0750
.
Profi le Setup Example
Sizing the burner and the corresponding profi le for a 5,000 SCFM and a 115 degrees
temperature rise.
1. Required BTU:
BTU/hr = Blower SCFM x Desired Temp. Rise x 1.08 / .92
BTU/hr =5,000 (SCFM) x 115 (∆T) x1.08 / .92 = 675,000 BTU/hr
2. Required Burner Length:
Feet of burner = [Required BTU/hr]÷[Burner Firing Rate (BTU/hr/ft)]
To determine the optimum burner length we can choose from a combination of 12 inch or 6 inch burner sections referring to Table 1. We can either fi re the burner at a rate of 675,000 BTU/hr per ft, or we can fi re the burner at 450,000 BTU/hr per ft (1.5 feet of burner). Refer to Chart 3 for the fuel pressures requirements at different fi ring rates.
3. Required Profi le Area:
Total Burner Area = Number of burner sections x burner area
(Burner Section) Burner Area 2 inch 0.11 sq. ft. 6 inch 0.32 sq. ft. 12 inch 0.65 sq. ft. T Section 0.77 sq. ft. Ell Section 0.65 sq. ft.
Total Burner Area = 1.0 (ft) x 0.65 = 0.650 ft Or Total Burner Area = 1.5 (ft) x 0.65 = 0.975 ft
6
Midco International Inc.
2
2
8471 34
Loading...
+ 12 hidden pages