ELIMINATING SALMONELLA IN THE FEED BY CONTROLLING CONDITIONER TEMPERATURE


        AL-Chalabi    Diyala Agricultural Sciences Journal, 7 ( 2 ) 44 – 58  ,2015 

  

 

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       CREATE AND EVALUATE A TEMPERATURE MONITORING SYSTEM IN THE 

CONDITIONER IN PELLETED FEED. 

Dhia AL-Chalabi* 

* Department of Agricultural machinery and equipment- College of Agriculture- University 

of Baghdad.  drdhia@coagri.uobaghdad.edu.iq 
  

ABSTRACT      

 

This project has been conducted in New Zealand in 1999, as a 

requirement for feed production companies to control salmonella in feed by 

Ministry of Agriculture and Fisheries (MAF). Feed is the most important factor 

in poultry production enterprises because of its impact on cost and health.  

It takes the feed about two minutes to reach the 80 ºC. The feed could be 

recycled if didn’t reach the 82-83 ºC planned. Steam temperature was stable and 

around 130 ºC. This temperature could be optimized to reduce energy cost 

without affecting the pelleting process through tracing the feed in temperature 

(ingredients) one can say, that some of the steam is entering to the feed-in tube 

and raising the feed-in temperature to 46-50 ºC. The regular incoming feed 

temperature was between 20-25 ºC. The die temperature was 92 ºC, and cooler 

temperature for the feed out was 20 ºC. 
Key words: Feed, Salmonella, pelleted feed, feed temperature, conditioner temperature, poultry feed. 

 

INTRODUCTION 

         Salmonella could be controlled in the conditioner when producing pelleted 

feed for poultry (Broilers, Turkey) or other animals. Feed temperature control in 

the conditioner is (Coony et al., 2010) one of the ways to eliminate salmonella 

and other bacteria in the feed manufacturing process (Himathongham et al.1996) 

practically and economically. The temperature range 80-85.7 C (McCapes et 

al., 1988) is affective to kill bacteria in the conditioner (Lake et al.,2005). The 

duration of the temperature is important as well (Africa Fernandez, 2003). 

Increasing the temperature above this range may drop feed nutritional value 

(Silverside, 1999) and may reduce the feed energy value (Creswell and Bedford, 

2006). Increasing the retention time may affect the productivity of the feed mill. 

Lower temperature could not affect bacteria present in the feed (John Payne, 

2001). Therefore it is essential to know what temperatures are in the conditioner 

(Peter Cressey, 2011), and or there are temperature differences in the 

conditioner. Monitoring feed temperature in two locations (in and out) is not 

enough to have a clear picture about the temperature in the conditioner. Because 

 ـــــــــــــــــــــــــــــــــــــــــــــــــــــــــــــــــــــ

Received for publication  27 / 10 / 2014. 

Accepted for publication  5 / 4 / 2015  . 



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 temperatures are usually varies from location to location in the conditioner 

especially with unstable run. Suggested pelleting feed temperature above 85 C 

should be avoided. 

Types of conditioners and coolers 

There are two major types of conditioners. The first one is that, the steam pipe 

connection is from the topside as well as the feed in tube. The second type is 

that the steam pipe is connected to the conditioner from bottom, and the feed in 

tube from top. Both of them may have retention plate installed at the end of 

conditioner cylinder.  

In the same time there are two types of coolers as well. First type is the counter 

flow cooler, where the air penetrates the feed from bottom to the top. The 

second one is the tower cooler. The air comes from the sides and exits from the 

bottom. Where the first one the sir comes from bottom and exits from top.  

Objectives 

1- Design and implement temperature monitoring system in the feed mill. 

2- Monitoring the feed temperature in the die will not exceed 92 C. 
3- Monitoring feed temperature inside the conditioner not the steam temp. 
4- Access to the system from any location through the internet. 
5- Display the data graphically and digitally by using Microsoft Office. 

 

METHODS AND MATERIALS 

This project has been conducted in New Zealand in 1999, as a requirement for 

feed production companies and to Salmonella control from Ministry of 

Agriculture and Fisheries (MAF). The temperature in the conditioner must be 

82.2 ºC in all parts of the conditioner (Wong , 2003). The system has to give a 

clear picture about the feed temperature during production. 

Instrumentation  

 To monitor inside temperature of the conditioner, depending on the length of 

the conditioner and the rotating mixing paddles inside the conditioner up to eight 

probes are needed in different locations to adequately collect data without 

damaging the probes. Locations of the probes are very important and critical to 

understand what is happening inside the conditioner. Many activities need to be 

clarified first; the connection of the steam pipe to the conditioner is one of them. 

Some conditioners are connected at the top others at the bottom. Probes should 

be placed in locations where the feed is moving, not the steam flow. This means 

that we are measuring the feed temperature not the steam temperature. Figure 1 

gives an idea about the locations of the probes. A data logger has been used with 

46 channels, the data logger connected to the internet though out a modem to 



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monitor the temperature and the data from any place in and out New Zealand. 

Probes used were thermocouples type T, installed though out the feed mill, to 

the control room, where the data collected and used to verify temperature pattern 

in all locations and to compare to the planned temperature according to MAF. 

 The probe locations are as follow: - 

1. Feed temperature, measures the feed (ingredients) temperature in the feed 
pipe connected to conditioner. (Probe 1 Figure 5). 

2. Steam in temperature, measures the steam temperature in the steam pipe 
connected to the conditioner Probe S. 

3. Bottom right feed temperature. (conditioner) 
4. Topside temperature to detect steam movement. (conditioner) 
5. Bottom left feed temperature. (conditioner) 
6. Bottom middle side feed temperature before exiting the conditioner. 
7. Feed out conditioner temperature, feed exiting the conditioner. 
8. Feed out the die temperature; feed temperature leaving the die to the 

cooler. 

Also we need at least 3 to 4 probes in the cooler to detect the feed temperature 

entering and leaving the cooler.  It is important to monitor feed temperature 

going to the feed storage bins. The above-suggested locations will give a good 

indication about the feed temperature and feed movement. Regarding to the 

movement of the feed and the steam distribution of probes was critical to reflect 

the correct and good mixing of the feed ingredients together and with the steam 

coming to the conditioner without any separation.  

Probe S will give us a clear idea about the steam temperature getting in the 

conditioner. Some times the steam temperature varies or fluctuates, and we are 

assuming that it is correct temperature. 

Probe 1 will give the temperature of the feed ingredients coming in the 

conditioner. This probe should always read lower temperature (20-30C), 

because there is no heating done to the feed ingredients in previous stages. 

Probes 2-6 will give an indication about the feed temperature changes and also 

how the feed is moving in the conditioner based on temperature changes. These 

probes should read temperatures range 80-85C.  

The topside probe 4 is an important probe in detecting steam flow especially in 

conditioners where the steam pipe is connected at the top. This probe will be at 

the left side of the feed in tube. If the temperature is in the range, then the flow 

is good, but if the temperature is low then the steam is entering the feed in tube, 

and it needs to be adjusted. See below diagram. 

Probe 7 gives the feed temperature leaving the conditioner. The temperature is 

just like in the conditioner.  

Probe 8 gives the pelleted feed temperature left the die (press). This temperature 

is usually above all temperature probes readings, because of the pressure 



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extracted on the feed and also the flow of the steam. This temperature could 

reach 92C, but it is for very short duration. 

 

Selecting method for adequate probes 

Selecting the right probe type and the adequate probe design is essential to 

collect valid data. Placing the probes in the conditioner is another important 

task. Probes should be in the place between the pedals of the rotating shaft. This 

is very delegate work and should be done by professionals.  

Missing one millimetre may destroy the prob. We should put in mind there is 

high temperature, feed moving and pedals rotating in the conditioner. The 

probes should withstand all of this. Probe should have the following 

specifications.  

Probe design 

1. Stainless steel body with raged smooth finish for easy cleaning. 
2. It should be fitted in a plastic or Teflon insulation plug to eliminate heat 

transfers for conditioner body temperature. 

3. Thermocouple or RTD probes could be used (preferably RTD). 

4. The range of the probe could be 0-120 C, and for the steam up to 200C. 
 

The plastic plug should have the following specifications. 

1. Very hard plastic, but not to be damaged when mounted in the 
conditioner. 

2. High temperature resistance. 
3. Easy to shape and work with. See figure 1 for more details.  

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Figure1. Probe specification design. 



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Figure2. Probes Placements and dimensions of the conditioner and coolers 

Numbers 2-8 are temperature probes in conditioner and 9-12 are temperature 

probes in the cooler. 
 

S 
6 

2720

Top View

8001150760

570

1000

3220

920

680

2620

600

90

180

370

640

2150
1600

1200
600

5

Top View

B

9

10

11

12

1060

240

850

90

10

7

8

B

Press

Feed Out

2

3

4

Pro bes Placeme nts
Condi rioner

Coo ler



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Figure 3. Tower cooler with temperature probes places. 
 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Outside Temperature

Feed Temperature

Air in

1
2

3

4

5

6

7

8

Probes Placem ent in the c ooler

Tow er Cooler  w ith temperature probes in

P E L L ET M IL L

C OOL E R

Overflow sensor

Level sensor

Feed in

FEED

AIR INAIR IN

WARM AIR

-

+

FEED OUT

W a rm  A Ir o u t

Outside normal Pressure 

Vacuumed 

Overflow sensor 

Level sensor 

Air in 



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Figure 4. Counter flow coolers showing air flow from bottom to top. 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Figure 5. Placement of the probes in the conditioner. 

 

Rules for probes temperature understanding 

Understanding the information from the data loggers; first we need to set the 

standards or rules for temperature goals inside and outside the conditioner. After 

that, we can monitor the temperature levels to achieve the bacterial control 

(Salmonella) or quality control (Williman, 2009). In general there are three 

groups or sets of temperatures we are looking for.  

1. First is the low temperature group, which is the feed (mixed ingredients) 
temperature before the conditioner (in the mixer or in the feed in tube). 

The temperature range is 20-25 C. It depends on storage and outside 

temperature as well. 

2. Second is the high temperature group, which is feed temperature in the 

conditioner. The temperature range is 80-85 C. The die temperature 

could reach 92C if above temperature is maintained (Ryszard Kuling, 

2008). 



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3. Third is the warm to cold temperature group, which is the feed (pelleted) 

temperature in the cooler. The temperature range is 20-75C.  See      

figure 6.  

The temperature categories and levels in the conditioner 

The next step is to monitor and control the feed temperature in these ranges 

and analyze the results.  Figures 7, 8, 9. 

 

Figure 6. Standard feed temperature in the conditioner. 

1. If the temperature of group 1 is higher than 30ºC.  
    This means that the steam is running to the feed mixer or to the feed 

tube. The   temperature may reach 50ºC. This happens a lot especially 

with conditioners having their steam pipe connected from the topside after 

the feed in tube, and also with other steam tube connection if the steam 

flows is restricted in the conditioner (more stem than the conditioner can 

handle). This situation could emerge when 

  The die is chocked-full with feed,  

  Bad start up or interrupted runs.  

Then the conditioner temperature will drop below the standard range. 

2. If the temperature of group 2 is lower than the range. This means  
 Some of the steam is running to the feed in tube. 

 Steam temperature is not enough to keep the conditioner temperature 

in the range. 

 Steam is not mixing with feed ingredients properly; steam pressure is 

low. 

 Probes may be faulty. 

S t a n d a r d  f e e d  t e m p e r a t u r e

0

1 0

2 0

3 0

4 0

5 0

6 0

7 0

8 0

9 0

1 0 0

M i x e r  t e m p . c o n d  1 c o n d  2 c o n d  3 c o n d  3 c o n d  4 c o n d  5 c o n d  6 d i e c o o l e r  1 c o o l e r  2 c o o l e r  3

L o c a t i o n

T
e

m
p

. 
C



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3. If the temperature of group 2 is higher than the range. This means. 
 The amount of steam is high. 

 Probes are exposed to direct steam flow. 

4. If the temperature of group 3 is above the standard range. This means 
 Over flow or temperature sensors are not working properly. 

 The vacuum in the cooler is not set properly. 

 Flow of feed is very high (feed is not losing heat or not cooling). 

 Exhaust duct is not clean (feed particles build up on the sides). 

RESULTS AND DISCUSSION 

There are two things to look at in the run. First is the startup temperature 

reaches the desired temperature. Second is the run or batch temperature. See 

Figure 7. It takes the feed about two minutes to reach the 80 ºC planned 

temperature. During that time 150-200 Kg (depend on conditioner capacity) of 

feed passes through the conditioner without reaching the desired temperature of 

80-85 ºC. This feed could be recycled so no feed will be allowed to go to the 

storage bins without reaching the planned or targeted temperature. Steadiness of 

the run has a great influence on the feed temperature in the conditioner. The 

more stops (On and off) in the run the more unstable temperature in the 

conditioner, and more feed going to the bins without reaching the planned 

temperature. This situation could be bad if salmonella was present in the feed or 

feed ingredients. This also means salmonella positive feed is been used to grow 

birds. The birds will be infected with salmonella whatever the bio-security is. 

Vaccination may help in situation like this.  

The batch run temperature is the most important factor affecting feed 

temperature. Figure 7 is showing the ideal run and the correct temperature in the 

conditioner. Looking at the graph from top, the steam temperature is stable and 

around 130ºC. This temperature could be optimized to reduce energy cost 

without affecting the pelleting process. To optimize temperature is to keep the 

temperature of the conditioner at its desired temperature and in the same time 

minimizing the heat loss from the conditioner to the room, where environmental 

temperature is usually lower. Insulating the conditioner by proper insulation will 

reduce or prevent heat loss, which keeps the conditioner temperature stable and 

that will reduce extra heat to keep the conditioner at its required temperature. 

Press (die) temperature is also stable and it is between 90-93 ºC. The Inside 

conditioner temperature (all probes) is in the same safe range of 82-83 ºC.  

The retention time in the cooler has also an important role in keeping the 

temperature longer. The top part of the cooler holds the feed temperature at 70-

75 ºC for about 5 minutes. This time allows the temperature to penetrate to the 

core of the feed pellet. The temperatures of the cooler are also in the safe range.



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Press (die) temperature is also stable and it is between 90-93 ºC. The Inside 

conditioner temperature (all probes) is in the same safe range of 82-83 ºC.  

The retention time in the cooler has also an important role in keeping the 

temperature longer. The top part of the cooler holds the feed temperature at 70-

75 ºC for about 5 minutes. This time allows the temperature to penetrate to the 

core of the feed pellet. The temperatures of the cooler are also in the safe range. 

The top cooler temperature (probe 9) is around 70ºC, the more we drop to the 

end of the cooler the more the temperature will drop, until it reaches 21.8ºC 

(feed temperature leaving to the storage bins).  

Also we can recognize that the air temperature could raise 3-4 º C inside the feed 

mill that is from the outside temperature (outside temperature 14.9 º C, air 

temperature entering the cooler is 18.9 º C). With air temperature rising relative 

humidity will decline (dryer air). This will dry the feed faster and losses 

moisture as well.  

Tracing the feed in temperature (ingredients) one can say, that some of the steam 

is entering to the feed-in tube (feed coming from the top, and the steam from 

bottom) and raising the feed-in temperature which supposed to be around 25 ºC. 

The incoming feed temperature is between 46-50 ºC. Steam going backward 

may cause problems in pipes and could cause condensation or crust formation 

on the sides. Losing steam to the incoming feed tube means there is not enough 

steam in the conditioner to reach the required temperature, and also means there 

is a problem in the system must solved and find out why the steam going back 

instead going in to conditioner. Figure 8 shows the temperature changes when 

the batch was controlled for feed mass flow. 

One of the serious problems in cleaning conditioners is the crust formation 

inside the conditioner figure 8. This problem is caused by the water 

condensation on the body of the conditioner especially in cold weather, when 

there is not enough time to preheat the conditioner before producing feed.  

 

The crust will trap small particles from feed and form a thick paste. This paste is 

not just trapping minerals and vitamins it may also be a good place for toxins 

and bacteria growth as well. 

The objectives of the project have been met and pelleted temperature was 

according to authority guidelines in New Zealand, figure 9. 

 

Recommendations 

 

1- To increase feed temperature at start-ups a retention plate may be placed in 
the conditioner or fully computerised system could be installed to monitor 

and control the start-up temperature in the conditioner at stops and start 

periods.  



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2- The temperature difference between outside and conditioner temperature is 
large, and to reduce that is to insulate the conditioner by proper and practical 

insulation to prevent crust formation and reduce heat loss. 

 

References 

 

Africa Fernandez-Gutierrez  and Ross breeders. 2003. Salmonella control in 

feedmills. Economic Evaluation of Defra Policy on Food-Borne 

Pathogens in Live Animals, Reading University, 

Cooney G.  2010. Turning up the heat with enzyme technology. Accessed at: 

http://www.allaboutfeed.net/article-database/turning-up-the-heat-with-

enzyme-technology-id1481.html. Accessed: 21 June 2010. 

Creswell D. and M. Bedford.  2006 .Effects of pelleting temperature of 

phytase supplemented broiler feed on tibia mineralization, calcium and 

phosphorus content of serum and performance. Czech J. Anim. Sci., 51, 2. 

78-84. 

Creswell D. and M. Bedford.  2006. High pelleting temperature reduces broiler 

performance. 2006. Aust. Poultry Sci. symp.1-6. 

Himathongkham S, das M Gracas Pereira, H Riemann.  1996. Heat destruction 

of Salmonella in poultry feed: Effect of time, temperature and moisture. 

Avian Diseases; 40: 72-77. 

Lake R, A. Hudson, P. Cressey, G. Bayne and N. Turner. 2005. Quantitative risk  

model: Salmonella spp. in the poultry food chain. ESR Client Report 

FW0546. Christchurch: ESR. 

John Payne, Wolter Rattink, Ted Smith and Tom Winowiski. 2001.   

The pelleting Handbook. Borregaard Lignotech. 10-13. 

McCapes R. H, H. E. Ekperiging., W. J. Cameron., W. L. Ritchie, J. Slagter, 

V. Stangeland  and  K. V Nagariaja. 1988. Effect of a new pelleting 

process on the level of contamination of poultry mash by Escherichia coli 

and Salmonella. Avian Diseases 33: 103-111. 

Peter Cressey, Andrew Hudson, Rob Lake, Sandra Moorhead. 

2011. Risk profile: Salmonella SPP. in animal feed Prepared for New 

Zealand Food Safety Authority under project MRP/08. 

Ryszard Kulig and Janusz Laskowski. 2008. Effect of conditioning 

parameters on pelle temperature and energy consumption in process of 

plant material pressing. Tekc Kom. Mot. Energ. Roln. – OL PAN, 8a, 

105-111. 

Silversides F. G. and M. R. Bedford. 1999. Effect of pelleting temperature on 

recovery and efficacy of a Xylanase enzyme in wheat based diets. Poultry 

Science, 78: 1184-1190. 

Wong T.L.2003. Survey of raw poultry in Christchurch to determine the 

prevalence of Salmonella Typhimurium DT1.ESR Client Report FW0321. 

Christchurch: ESR. 

http://www.allaboutfeed.net/article-database/turning-up-the-heat-with-
http://www.allaboutfeed.net/article-database/turning-up-the-heat-with-


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Williman J., E. Lim, R. Pirie, P. Cressey  and R. Luke. 2009. Annual report 

concerning foodborne disease in New Zealand 2008. ESRClinet Report 

FW09062. Christchurch: ESR. 

 

 

 . لحبيبيا تقيين نظام هراقبت لدرجاث الحرارة في هكيف العلف وأنشاء 

    *ألجلبي هحود احود ضياء

 drdhia@coagri.uobaghdad.edu.iq -جايعح تغذاد  - كهيح انضساعح –قسى انًكائٍ ٔ انًعذاخ انضساعيح  -يساعذ أسرار*

  

 الوستخلص

طهة يٍ ٔصاسج انضساعح ٔ انثشٔج انسًكيح انُيٕصيالَذيح ت َذفي َيٕصيال 9111ذى ْزا انعًم في عاو         

شاسج ففي يكيف  انعهف  نًشاقثح انسهًَٕيال في انعهف  كفرجشال نًعفُعي افعفالت نهرركفذ يفٍ اٌ دسجفح ان ف

ْفٕ أْفى عايفم  و في كم افٔقاخ ٔ في جًيع افياكٍ داخم انًكي  انعهففي  نٌ انعهف  º :2ان ثيثي ذكٌٕ 

ح تعفٕسج انعف نرفاني عهفى ذكفاني   افَرفاج ٔاتسثة أثشِ عهى أٔصاٌ انطيٕس ٔ ت في نَراج انذٔاجٍ ٔرنك

 عايح  

 º;2-:2نفى يثهف   نفز يًكٍ نعادج ذذٔيشانعه  ن نر  و 28ºيسرغشق انعه  حٕاني دقيقريٍ نهٕصٕل انى      

كثيفش عهفى ثثفاخ دسجفاخ حفشاسج انعهف   ففي ٔافَراج نّ ذرثيش سهثي عًهيح اثُال انًسرًشج   أٌ انرٕقفاخ  و

ٔعُفذ عفذو ٔصفٕل و انفى حفٕاني دقيقرفيٍ   28ºيكي  انعه    ي راج انعهف  نهٕصفٕل انفى دسجفح حفشاسج 

   كاَد دسجفح ان فشاسج انثخفاس يسفرقشج فرَّ يعاد ذذٔيشِو   º;2 -:2دسجح حشاسج انعه  انًخطط نٓا انى 

جعم دسجفح حفشاسج يكيف  انعهف  يثانيفح  نرقهيفم ذكهففح انطاقفح و  تافيكاٌ º 8;9حٕاني ْٔي ، اثُال انعًم

يًكفٍ انقفٕل أٌ تعفن يفٍ نر دٌٔ انررثيش عهى عًهيح ذعُيع انعه   يٍ خالل ذعقة دسجفح حفشاسج انعهف  

)انُفاصل  في دسجح حشاسج خهيط انعه  انذاخم  أسذفاعانثخاس يذخم في أَثٕب انرغزيح نهعه  يًا يؤد  انى 

تفيٍ  دَفكا   اٌ دسجح حشاسج انعه  انفذاخم نًكيف  انعهف  ان ثيثفي  وº 8=-<>انى  ثينًكي  انعه  ان ثي

:8-:= º1فففي قانففة ان ثيثففاخ كاَففد أيففا دسجففح ان ففشاسج   و: º ٍو   ٔ دسجففح ان ففشاسج انعهفف  انخففاسج يفف

 و    º 8:صُذٔق انرثشيذ انعهفي كاَد 
 

 جح حشاسج يكث  انعه  ان ثيثي  عه  انذٔاجٍعه    عه  حثيثي  دسجح حشاسج انعه   دس الكلواث الوفتاحيت: