Author Archives: medical-waste-incinerator
Double Combustion Chamber Containerized Mobile Incinerator
Waste Incinerator Mounted in ISO 20′ or 40′ Container before leave Factory. Regular Waste Burning Rate from 10kgs to 150kgs per hour.
Double Combustion Chamber
The incinerator design with primary combustion chamber, secondary combustion chamber(post combustion) and dry scrubber optional. This design will reduce black smoke, burn completely and Environmentally Friendly.
Free Installation
The incinerator mounted already in the container, complete with fuel system, electric system and the control case fixed already. Fix chimney and connect electric will be ready for operation.
Mobile Incinerator
Waste Incinerator Mounted in ISO 20′ or 40′ Container. It’s moveable with truck to anywhere or emergency requirement.
Containerized Incinerator
Rate: upto 150kgs per hour
Containerized Incinerator: we delivery incinerator and also container to customers, no requirement to build incineration house.
Double Combustion Chamber
Combustion Chamber: upto 1500Liters
Primary combustion for waste feeding and burning and secondary combustion to burn smoke only.
Incinerator Moveable by truck
Amount weight: 4Ton to 9Ton
Mobile function to anywhere or service to customer at their local site.
Programme on Small Scale Medical Waste Incinerators for Primary Health Care Clinics
TABLE OF CONTENTS
- OBJECTIVE OF THE PROGRAMME 4
- STRUCTURE OF THE PROGRAMME 4
- COLLABORATORS INVOLVED IN THE PROGRAMME 4
- STAKEHOLDERS INVOLVED IN THE PROGRAMME 4
- LABORATORY TRIALS 5
- FIELD TRIALS 13
1. OBJECTIVE OF THE PROGRAMME
The objective of the programme is to select technical criteria suitable for tender specification purposes that will enable the South African Department of Health to obtain the services and equipment necessary for the primary health care clinics to carry out small-scale incineration for the disposal of medical waste.
2. STRUCTURE OF THE PROGRAMME
The test programme is being carried out in phases, as follows:
Phase 1 A scoping study to decide the responsibility of the different parties and
consensus on the test criteria and boundaries of the laboratory tests. The criteria for accepting an incinerator on trial was approved by all parties involved.
Phase 2 Laboratory tests with a ranking of each incinerator and the selection of the incinerators to be used in the field trials.
Phase 3 Completion of field trials, to assess the effectiveness of each incinerator under field conditions.
Phase 4 Preparation of a tender specification and recommendations to the DoH for the implementation of an ongoing incineration programme.
This document provides feedback on phases 2 and 3 of the work.
3. COLLABORATORS INVOLVED IN THE PROGRAMME
SA Collaborative Centre for Cold Chain Management SA National Department of Health
CSIR
Pharmaceutical Society of SA World Health Organisation UNICEF
4. STAKEHOLDERS INVOLVED IN THE PROGRAMME
The following stakeholders participated in the steering committee:
- Dept of Health (National & provincial levels) (DoH)
- Dept of Occupational Health & Safety (National & provincial levels)
- Dept of Environmental Affairs & Tourism (National & provincial levels) (DEAT)
- Dept of Water Affairs & Forestry (National & provincial levels) (DWAF)
- Dept of Labour (National & provincial levels) (DoL)
- National Waste Management Strategy Group
- SA Local Government Association (SALGA)
- SA National Civics Organisation (SANCO)
- National Education, Health and Allied Workers Union (NEHAWU)
- Democratic Nurses Organisation of SA (DENOSA)
- Medecins Sans Frontieres
- SA Association of Community Pharmacists
- Mamelodi Community Health Committee
- Pharmaceutical Society of SA
- CSIR
- UNICEF
- WHO
- SA Federation of Hospital Engineers
International visitors:
- Dr Luiz Diaz – WHO Geneva and International Waste Management , USA
- Mr Joost van den Noortgate – Medecins Sans Frontieres, Belgium
5. LABORATORY TRIALS
5.1. Objective of the laboratory trials
- Rank the performance of submitted units to the following criteria:
y Occupational safety
y Impact on public health from emissions
y The destruction efficiency
y The usability for the available staff
- The panel of experts for the ranking consisted of a:
y Professional nurse; Mrs Dorette Kotze from the SA National Department of Health
y Emission specialist; Dr Dave Rogers from the CSIR
y Combustion Engineer; Mr Brian North from the CSIR
5.2. Incinerators received for evaluation
Name used in report | Model no. | Description | Manufacturer |
C&S Marketing
incinerator |
SafeWaste Model Turbo
2000Vi |
Electrically operated fan supplies combustion air
– no auxiliary fuel |
C&S Marketing cc. |
Molope Gas incinerator | Medcin 400 Medical
Waste Incinerator |
Gas-fired incinerator | Molope Integrated
Waste Management |
Molope Auto incinerator | Molope Auto Medical
Waste Incinerator |
Auto-combust incinerator – uses wood
or coal as additional fuel to facilitate incineration |
Molope Integrated
Waste Management |
Name used in report | Model no. | Description | Manufacturer |
PaHuOy
incinerator |
Turbo Stove | Auto-combust unit,
using no additional fuel or forced air supply |
Pa-Hu Oy |
5.3. Emission testing: laboratory method
Sampling of emissions followed the US-EPA Method 5G dilution tunnel method for stove emissions. Adjustments to the design were made to account for flames extending up to 0.5 m above the tip of the incinerator and the drop out of large pieces of ash. Emissions were extracted into a duct for isokinetic sampling of particulate emissions. The sampling arrangement is shown by a schematic in Figure 1. A photograph of the operation over the Molope gas fired incinerator unit is shown in Figure 2.
All tests were performed according to specified operating procedures. The instructions provided by the supplier of the equipment were followed in the case of the C&S Marketing Unit. No operating procedures were supplied with the Molope Gas, Molope auto-combustion and PaHuOy units. These procedures were established by the CSIR personnel using their previous experience together with information provided by the supplier.
Test facilities were set up at the CSIR and measurements were carried out under an ISO9001 system using standard EPA test procedures or modifications made at the CSIR.
Figure 1. Schematic diagram of the laboratory set-up
Figure 2:Photograph of air intake sampling hood over Molope gas incinerator
5.4. RANKING RESULTS OF THE LABORATORY TRIALS
Using the criteria listed under section 4.1 above, the incinerators were ranked as followed:
Molope gas-fired
unit |
Molope wood-fired
unit |
C&S electric
unit |
PaHuOy wood-fired
unit |
|
Safety | 6.8 | 4.8 | 5.5 | 3.3 |
Health | 5.5 | 3.5 | 4.3 | 2.3 |
Destruction | 9 | 2 | 6 | 1 |
Usability | 2 | 3 | 3 | 5 |
Average | 5.8 | 3.3 | 4.7 | 2.9 |
5.5. EMISSION RESULTS OF THE LABORATORY TRIALS
Quantitative measurements were used to rank the units in terms of destruction efficiency and the potential to produce hazardous emissions.
Conformance to the South African Department of Environmental Affairs and Tourism’s (DEAT) recommended guidelines on emissions from Large Scale Medical Waste Incinerators is summarized in Table 1. The measurements are listed1 in Table 2.
Table 1: Summary qualitative results
Parameter Measured | Units | Molope
Gas-fired |
Molope
Wood-fired |
C&S
Electric |
PaHuOy
Wood-fired |
SA DEAT
Guidelines |
Stack height | m | × | × | × | × | 3 m above
nearest building |
Gas velocity | m/s | × | × | × | × | 10 |
Residence time | s | × | × | × | × | 2 |
Minimum combustion
temperature |
ºC | 4 | × | × | × | > 850 |
Gas combustion
efficiency |
% | × | × | × | × | 99.99 |
Particulate emissions | mg/Nm3 | 4 | × | 4 | × | 180 |
Cl as HCl | mg/Nm3 | × | 4 | 4 | × | < 30 |
F as HF | mg/Nm3 | 4 | 4 | 4 | 4 | < 30 |
Metals | mg/Nm3 | 4 | × | × | 4 | < 0.5 and
< 0.05 |
1 Emission concentrations are reported in accordance with the South African reporting requirements, ie, normalized to Normal Temperature (0
oC) and Pressure (101.3 kPa) and corrected to a nominal concentration of
8 % of CO2 on a dry gas basis. If a measurement fell below the detection limit for the method is it either reported as the detection limit or as N.D., ie, not detectable.
Table 2: Detailed quantitative results
Parameter Measured * |
Units |
Molope gas |
Molope auto |
C&S |
PaHuOy |
SA Process Guide1 |
Comments |
Stack height |
m |
1.8 |
1.8 |
1.9 |
0.3 |
3 m above nearest building |
None of these unite has a stack. The height of the exhaust vent is taken as the stack height. If it is above the respiration zone of the operator it provides some protection from exposure to smoke. |
Gas velocity |
m/s |
0.8 |
0.5 |
1.1 |
0.5 |
10 |
Gas velocities vary across the stack for the Molope gas, Molope auto-combustion, and the PaHuOy units. |
Residence time |
s |
0.4 |
0.7 |
0.6 |
0.4 |
2 |
Residence time is taken to be the total combustion time, and the maximum achievable |
Minimum combustion zone temperature |
oC |
800 -900 |
400 – 650 |
600 – 800 |
500 – 700 |
> 850 |
Molope auto-combustion temperatures are expected to be higher as the centre of the combustion zone is not expected to be at the measurement location. |
CO2 at the stack tip |
% vol |
2.64 |
3.75 |
4.9 |
3.25 |
8.0 |
Actual emission concentrations are less than the values reported here, which are normalized to 8 % CO2 and Normal temperature and pressure for reporting purposes. They are lower between 4 to 8 times. |
Gas |
% |
99.91- |
98.8 -98.4 |
99.69- |
98.9 |
99.99 |
Most accurate measurement in |
Combustion | 99.70 | 99.03 | the duct where mixing of exhaust | ||||
efficiency | gases is complete. Results of two
trials. |
||||||
Particulate emissions entrained in exhaust gas |
mg/Nm3 |
102 |
197 |
130 |
338 |
180 |
The total emissions are the sum of the both entrained and un- entrained particulates. Emissions are lower than expected for such units and this is attributed to the absence of raking which is the major source of particulate emissions from incinerators without an emission control system. |
Particulate fall- out |
mg/Nm3 |
42 |
105 |
n.d. |
n.d. |
– |
Large pieces of paper and cardboard ash rained out of the emissions. Totalling 0.8 to 2 g over a +/- 2 minute period. |
Soot in particulates |
% |
42.2 |
58.1 |
48.7 |
84.8 |
– |
Correlates directly with gas combustion efficiency |
1 Emission concentrations are reported in accordance with the South African reporting requirements, ie, Normalized to Normal Temperature (0
oC) and Pressure (101.3 kPa) and corrected to a nominal concentration of
8 % of CO2 on a dry gas basis. If a measurement fell below the detection limit for the method is it either reported as the detection limit or as N.D., ie, not detectable.
Parameter Measured * |
Units |
Molope gas |
Molope auto |
C&S |
PaHuOy |
SA Process Guide1 |
Comments |
% ash residual from medical waste |
% |
14.8 |
12.9 |
15.6 |
21.7 |
– |
Measurement of destruction efficiency of the incinerator. Typical commercial units operate at 85-90 % mass reduction. PaHuOy is lower due to the melting and unburnt plastic. |
Cl as HCl |
mg/Nm3 |
46 |
13 |
25 |
35 & 542 |
< 30 |
PaHuOy chloride concentrations varied considerably. This is expected due to the variability of the feed composition. |
F as HF |
mg/Nm3 |
< 6 |
< 1 |
<2 |
< 1 |
< 30 |
Fluoride not found in this waste. |
Arsenic (As) |
mg/Nm3 |
< 0.2 |
< 0.2 |
< 0.2 |
< 0.2 |
0.5 |
Arsenic is not expected as a solid. |
Lead (Pb) |
mg/Nm3 |
< 0.4 |
< 0.4 |
< 0.4 |
< 0.4 |
0.5 |
Lead not expected in waste |
Cadmium (Cd) |
mg/Nm3 |
< 0.2 |
< 0.2 |
< 0.2 |
< 0.2 |
0.05 |
Sensitivity of the x-ray method is adequate for ranking. Higher sensitivity not sought for this trial. |
Chromium (Cr) |
mg/Nm3 |
< 0.1 |
0.7 |
0.7 |
< 0.1. |
0.5 |
Chromium relative to iron ranges between 12 and 25% which is consistent with stainless steel needles |
Manganese (Mn) |
mg/Nm3 |
< 0.1 |
0.3 |
0.3 |
< 0.1 |
0.5 |
Manganese may be a component in the stainless steel needle. |
Nickel (Ni) |
mg/Nm3 |
< 0.1 |
0.3 |
< 0.1 |
< 0.1 |
0.5 |
Nickel may be a component in the needle. |
Antimony (Sb) |
mg/Nm3 |
< 0.2 |
< 0.2 |
< 0.2 |
< 0.2 |
0.5 |
Not expected in this waste. |
Barium (Ba) |
mg/Nm3 |
< 0.5 |
< 0.5 |
< 0.5 |
< 0.5 |
0.5 |
Lower sensitivity due to presence in the filter material |
Silver (Ag) |
mg/Nm3 |
< 0.2 |
< 0.2 |
< 0.2 |
< 0.2 |
0.5 |
Not expected in this waste. |
Cobalt (Co) |
mg/Nm3 |
< 0.1 |
< 0.1 |
< 0.1 |
< 0.1 |
0.5 |
Cobalt might be present in stainless steel. |
Copper (Cu) |
mg/Nm3 |
< 0.5 |
< 0.5 |
< 0.5 |
< 0.5 |
0.5 |
Lower sensitivity due to copper in the sample blanks. May be background in the analytical equipment. |
Tin (Sn) |
mg/Nm3 |
< 0.2 |
< 0.2 |
< 0.2 |
< 0.2 |
0.5 |
Tin not expected in this waste. |
Vanadium (V) |
mg/Nm3 |
< 0.1 |
< 0.1 |
0.4 |
< 0.1 |
0.5 |
Vanadium might be present in stainless steel. |
Thallium (Tl) |
mg/Nm3 |
< 0.4 |
< 0.4 |
< 0.4 |
< 0.4 |
0.05 |
Not expected in this waste. Sensitivity of the x-ray method is adequate for ranking. Higher sensitivity not sought for this trial. |
5.6. MAIN FINDINGS OF THE LABORATORY TRIALS
The main conclusions drawn from the trials are as follows:
::: All four units can be used to render medical waste non-infectious, and to destroy syringes or render needles unsuitable for reuse.
::: The largest potential health hazard arises from the emissions of smoke and soot. (the combustion efficiency of all units lies outside the
regulatory standards). The risk to health can be reduced by training operators to avoid the smoke or by installation of a chimney at the site.
::: The emissions from small scale incinerators are expected to be lower than those from a wood fire, but higher than a conventional fire-brick-
lined multi-chambered incinerator.
::: Incomplete combustion, and the substantial formation of smoke at low height rendered the PaHuOy unit unacceptable for field trials. Figure 3
below shows this unit during a trial burn. Molten plastic flowed out of
the incinerator, blocked the primary combustion air feed vents, and burnt outside of the unit.
Figure 3: Photo of PaHuOy incinerator during trial burn
5.7. COMPARISON OF THE FIELDS TRIALS WITH THE LABORATORY TRIALS
The CSIR performed a quantitative trial in the field for gas combustion efficiency, temperature profiles and mass destruction rate on the Molope Auto wood-fired unit at the Mogale Clinic.
The results of this trial are compared to the laboratory trial results below:
- Waste loading: Disposable rubber gloves were observed in addition to needles syringes, glass vials, bandages, dressings, and paper w
- Temperatures and combustion efficiency: The same performance in gas combustion efficiency was obtained for wood .
Temperatures were higher but for a shorter time and this was
correlated with the type of wood available to the clinic. The fuel was burnt out before the medical waste was destroyed completely and this resulted in lower temperatures, lower combustion efficiency and higher emissions while burning the waste.
- Emissions: Large amounts of black smoke were observed and this was correlated directly to cooling of the unit as the wood fuel was exhausted
prior to full ignition of the waste.
- Destruction efficiency: The destruction efficiency was similar to that in the laboratory measurem
- Usability: The unit is difficult to control as the result of the variability of the quality of wood
- Acceptability: the smoke was not acceptable to the clinic, the community, or the local
It was concluded that:
- The performance with fuel alone indicates that laboratory trial data can be used to predict emissions in the
- The Molope Auto unit is too difficult to control for the available staff and fuel at the
5.8. RECOMMENDATIONS FROM THE LABORATORY TRIALS
The following recommendations are made as the result of the laboratory trials:
::: A comprehensive operating manual must be supplied with each unit.
Adequate training in the operation of the units must be provided, especially focussed on safety issues.
::: It is recommended that the height of the exhaust vent on all units be
addressed. In order to facilitate the dispersion of emissions and reduce the exposure risk of the operators.
::: The suppliers of the incinerators must provide instructions for the safe handling and disposal of ash.
5.9. RECOMMENDATIONS FROM THE STEERING COMMITTEE
After completion of the laboratory trials, the project steering committee recommended that the Molope Gas and C&S Marketing units be submitted for field testing. The Molope Auto was recommended for field testing on the condition that the manufacturer modified the ash grate so as to prevent the spillage of partially burnt needles and syringes.
6. FIELD TRIALS
6.1. OBJECTIVE OF THE FIELD TRIALS
The objective of the field trials was to obtain information in the field and assess the strengths and weaknesses of each of the incinerators during use at primary health care clinics.
A participative decision making process was used for the trials. It was based on expert technical evaluation by the CSIR and the National Department of Health as well as participation in the trials by experienced end users and participating advisors. All decisions were made by the Steering Committee, which consisted of representatives of stakeholders in the clinical and medical waste disposal process. These included representatives from the National, Provincial, and Local Government departments of Health, Safety and the Environment, as well as Professional Associations, Unions, NGOs, UNICEF, the WHO and local community representatives.
6.2. CLINIC SELECTION
The Provinces in which the trials were done selected clinics for the field trials. The criteria set by the Steering Committee for the selection of the clinics were the following:
- Location must be rural or under-serviced with
y No medical waste removal
y No existing incineration
y No transport
- It must be in a high-density population area
- Acceptable environmental conditions must prevail
- Community acceptance must be obtained
- Operator skill level to be used must be at a level of illiteracy
The clinics that were selected were as follows:
- Steinkopf Clinic – Northern Cape Province – Gas incinerator
- Marydale Clinic – Northern Cape Province – Gas incinerator
- Mogale Clinic – Gauteng Province – Auto combustion
incinerator, wood-fired.
- Chwezi Clinic – KwaZulu-Natal Province – Gas incinerator
- Ethembeni Clinic- KwaZulu-Natal Province – Auto-combustion electrical
incinerator
MAP OF SOUTH AFRICA INDICATING WHERE THE CLINICS ARE SITUATED
NORTHERN PROVINCE
GAUTENG PROVINCE
NORTH WEST PROVINCE
MPUMALANGA PROVINCE
FREE STATE PROVINCE
NORTHERN CAPE PROVINCE
KWAZULU-NATAL PROVINCE
|
EASTERN CAPE PROVINCE
WESTERN CAPE PROVINCE
6.3. COORDINATION OF THE TRIALS
The criteria for the ranking of the incinerators in accordance with performance in the field were:
- Safety (occupational and public health)
- Destruction capability
- Usability
- Community acceptability
The South African National Department of Health coordinated the field trials.
Information regarding the field trials as well as questionnaires were supplied to the coordinators in the participating provinces.
The team in the field consisted of the operator, supervisor and inspector (coordinator). The manufacturer of the incinerators did the training of the operators.
The questionnaires used during the trials were set so as to obtain information with regard to the criteria set for the ranking of the incinerators in accordance with performance in the field. The questionnaires were received from the clinics at two-weekly intervals.
Questions with regard to the criteria were the following:
A. SAFETY (occupational and public health)
- Smoke Emission
y Volume and thickness
y Colour
y Odour
- Ash Content
- Are the filled sharps boxes and soiled dressings stored in a locked location while waiting to be incinerated?
B. DESTRUCTION CAPABILITY
- Destruction Rate
y Complete
y Partial
y Minimal
y Residue content
C. USABILITY (for the available staff)
- Can the incinerator be used easily?
- Is the process of incineration safe?
- Has training been successful?
- Is protective clothing such as gloves, goggles, dust masks and safety boots available?
D. COMMUNITY ACCEPTABILITY
- What is the opinion of the following persons on the use of the incinerator?
y Operator
y Nurse
y Head of the clinic
y Local Authority representative
y Community leader
During the trials the clinics were visited and the incinerators evaluated by members of the Steering Committee and the CSIR as well as Dr L Diaz from WHO, Mr M Lainejoki from UNICEF and the coordinator from the National Department of Health.
6.4. QUESTIONNAIRE RESULTS
6.4.1. MOGALE CLINIC
Type of incinerator at the clinic: Molope Auto-Combustion (Fired with wood)
Figure 4 & 5: Molope Auto wood-fired incinerator during field trials at Mogale clinic
A. SAFETY (occupational and public health)
- The process of incineration with this unit was considered by the operator, supervisor and the inspector as unsafe because there is no protective cage around the During the process the incinerator becomes very hot and this could result in injury to the operator.
- The smoke emission of this incinerator had a volume and thickness which was heavy and black, with a distinct unpleasant odour, and was considered This could cause a pollution problem.
B. DESTRUCTION CAPABILITY
- The needles and vials were not completely destroyed but were rendered unsuitable for re-use.
- The soft medical waste was completely destroy
C. USABILITY
Difficulty in controlling the operating temperature and avoiding smoke emissions made this incinerator user unfriendly.
D. COMMUNITY ACCEPTABILITY
As a result of the heavy, black smoke emission the unit was not acceptable to the community.
6.4.2. ETHEMBENI CLINIC:
Figure 6: C&S Marketing Auto Combust Electrical Incinerator At Ethembeni Clinic
Type Of Incinerator: C&S Auto-Combustion (Uses an electrically actuated fan)
A. SAFETY (occupational and public health)
- The operator, supervisor and inspector considered this incinerator easy to operate with no danger to the Removal of the ash from the drum for disposal in a pit is, however, considered difficult, as the drum is heavy. Removal of the incinerator lid before it has been allowed to cool has been identified as a potential danger to the operator.
- Emission of smoke from this incinerator was not considered ex The volume and thickness was evaluated as moderate with no pollution experienced.
B. DESTRUCTION CAPABILITY
- The needles and vials were not completely destroyed but were rendered unsuitable for re-use.
- The soft medical waste was completely destroy
C. USABILITY
Considered user friendly by operator, supervisor and inspector.
D. COMMUNITY ACCEPTABILITY
The incinerator was accepted by the community and was not considered to be harmful.
6.4.3. CHWEZI CLINIC, MARYDALE CLINIC AND STEINKOPF CLINIC:
Type of incinerator: Molope Gas incinerator
Figure 7: Molope Gas incinerator during field trials at Marydale clinic
A. SAFETY (occupational and public health)
- The operator, supervisor and inspector considered this incinerator easy to operate with minimal danger to the
- Smoke emissions were not excessive and were reported to be minim
B. DESTRUCTION CAPABILITY
- Sharps not completely destroyed but were rendered unsuitable for re-use.
- Soft medical waste completely destroy
C. USABILITY
This incinerator was considered user friendly.
D. COMMUNITY ACCEPTABILITY
The incinerator was accepted by the community and was not considered to be harmful.
6.5. RANKING
INCINERATOR | RANKING |
Molope Gas | 1 |
C&S Auto-Combustion (Uses electrical fan) |
2 |
Molope Auto- Combustion (Fired with
wood, coal also an option) |
3 |
6.6. OUTCOME OF THE FIELD TRIALS
Incinerator | Safety | Destruction Capability | Usability | Community Acceptability |
Molope Gas | Good | Good | Good | Good |
C&S Auto- Combustion
(Uses Electricity) |
Good |
Good |
Good |
Good |
Molope Auto-
Combust Incinerator |
Un-Acceptable | Good | Un-Acceptable | Un-Acceptable |
BIO WASTE INCINERATOR
50 kg/ hour capacity incinerators
· Burning Rate: 50kos/hr
· Feed Capacity: 150kqs
· Primary Combustion Chamber: 900 liters
· Secondary Combustion Chamber: 300 liters
· Mix Combustion Chamber: Yes
· Smoke Filter Chamber: Yes
· Feed Mode: Manual
· Power: 0.7Kw
· Fuel Type: Diesel Oil/ Natural Gas/LPG
· Internal Dimensions: 120 x 90 x 85cm (primary chamber)
· External Dimensions: 200 x 160 x 310cm (without chimney)
· Burning Efficiency: >98%
small scale medical waste incinerators.The required burning capacity of those incinerators are 10 kg and 15 kg/hr .The fuel oil using for those incinerator is diesel oil .
Hot Medical Waste Disposing Machine Burn rate per hour: 250 -300kg/hr

Type |
Pyrolytic:- Hot Medical Waste Disposing Machine |
Operation Condition |
8-16 Hr /day |
Controls |
Built in data recording |
Incinerator |
Type: continuous loading |
Capacity/Burn rate per hour: 250 -300kg/hr |
|
Temperature: 900-1200 oC |
|
Material: External- 3 layers Internal lining: a fire proof material of pre-fired refractory bricks with Aluminium lining, resistant to corrosive waste or gas and to thermal shock |
|
Secondary |
Type: horizontal/vertical |
Temperature: 1200-1400 oC |
|
Residence time of gases : >2 seconds |
|
|
Material External- Low thermal mass insulation 14-30 oC Internal lining: a fire proof material of pre-fired refractory bricks with Aluminium nettle lining, resistant to corrosive waste or gas and to thermal shock. |
Ash Handling System |
Both Automatic and manual removal of Ash. Must ensure removal/treatment of hazardous remnants of ash. |
Flue gas treatment system |
Capable of treating the flow of flue gas as the incinerator is operating at its maximum capacity |
Auxiliary device: Water level gauge, pressure sensor, PH sensor..etc. |
|
Auxiliary device: Fuel cut off device |
|
Waste feeding mechanism |
Automatic pneumatic/hydraulic waste loading system or conveyor belt , capacity 650-800L at a time |
Chimney (Stack) |
Type: Vertical type |
height: 7-10 meters |
|
Material: Fireproof cast, stainless steel |
|
Wet scrubbing system |
Vertical sprat tower with baffles or packing inside |
Gas emission |
Reduction of Pollutant gas SO2, HCL, HF and line particulate |
OUTPUT |
ASH -Max <5% of original waste size |
GAS- SMOKELESS,ODORLESS |
|
Emission standard |
WHO/ European |
Test report for emission testing |
Must be provided |
Product Data sheet/ Catalogue |
Must be attached to the ITB |
Additional Requirement |
– Local agent or branch in Ethiopia – Training for users as well as for EPHI maintenance staff on preventive maintenance – Fuel tanker with a minimum capacity of 2500 litre (made of plastic material with overfill prevention valve ,fuel gauge, lifting eyes) – The bidder should be willing to sign at least a five years’ service and maintenance agreement with the client (EPHI) – The supplier shall arrange by itself lifting equipment and labour needed during the installation, testing and commissioning of the incinerator |
incinerators at three facilities to process healthcare waste
a. 2.5 metric tons per day healthcare waste incinerator
b. 1.5 metric tons per day healthcare waste incinerator
c. 300 kg per day healthcare waste incinerator
Our preferred technology is double-chamber incineration, but if you recommend an alternative technology, that is acceptable as well.
We request information on the following for each of the above requirements:
1. Capital cost (delivered cost in Oman)
2. Operation and maintenance costs (per year)
3. Number of operators required
4. Product specifications (sizes, temperatures, residence time, cycle time etc)
5. Other auxiliary equipment that is required or recommended by you
HICLOVER TS Model Incinerator
Email: [email protected]

|
HICLOVER Incinerator/Parts Range |
Main Feature |
Medical Waste Incinerators |
HICLOVER 10-500kgs/Hr.Double Combustion Chambers |
Single Combustion Chamber |
Small, Cheap,10-20kgs/Hr. |
Three Combustion Chambers(Optional) |
3 Ranked for high risk waste |
Pet Cremation Equipment |
For Pet(small/big) Cremation Business |
Animal Incineration Equipment |
For additional creature incineration
|
Items/Model |
TS100(PLC) |
TS150(PLC) |
TS300(PLC) |
TS500(PLC) |
Burn Rate (Typical ) |
100 kg/hour |
150 kg/hour |
300 kg/hour |
500 kg/hour |
Control Mode |
PLC Auto. |
PLC Auto. |
PLC Auto. |
Combustion Chamber |
1200L |
1500L |
2000L |
3000L |
Internal Dimensions |
120x100x100cm |
150x100x100cm |
170x120x100cm |
210x120x120cm |
Secondary Chamber |
600L |
750L |
1000L |
1500L |
Smoke Filter Chamber |
Dry Scrubber |
Dry Scrubber |
Dry Scrubber |
Dry Scrubber |
Feed Mode |
Manual |
Manual |
Manual |
Manual |
Voltage |
220V |
220V |
220V |
220V |
Power |
1.38Kw |
1.69Kw |
2.57Kw |
4.88Kw |
Diesel Oil Consumption (kg/hour) |
Ave.20.4 |
Ave.24.2 |
Ave.33 |
Ave.44 |
Natural Gas Consumption (m3n/hour) |
Ave.24.5 |
Ave.29 |
Ave.39.6 |
Ave.52.8 |
Infection Monitor |
Yes |
Yes |
Yes |
Yes |
Temperature Protection |
Yes |
Yes |
Yes |
Yes |
Oil Tank |
200L |
300L |
500L |
500L |
Chimney |
10Meter |
10Meter |
14Meter |
14Meter |
Chimney Type |
Stainless Steel |
Stainless Steel |
Stainless Steel |
Stainless Steel |
1st. Chamber Temperature |
800℃–1000℃ |
800℃–1000℃ |
800℃–1000℃ |
800℃–1000℃ |
2nd. Chamber Temperature |
1000℃-1200℃ |
1000℃-1200℃ |
1000℃-1200℃ |
1000℃-1200℃ |
Residency Time |
2.0 Sec. |
2.0 Sec. |
2.0 Sec. |
2.0 Sec. |
Gross Weight |
6000kg |
8500kg |
11000kg |
16000kg |
External Dimensions |
260x150x180cm |
300x160x190cm |
400x210x300cm |
450x210x300cm |
2020-09-17
INCINERATOR TESTING AND COMMISSIONING
A flue chimney, 15,000mm long and 560mm diameter shall be constructed from steel sheet, complete with lagging, damper and rain water protection cone. The chimney shall be lined with castable grade diatomaceous concrete mixed with high alumina cement in accordance with BS 4076: 1989.
The damper will control the closing of the door to not less than 85%. The stack is to allow fresh air at the stock’s base so that the flue gases are discharged at not move then 4000 C and that the discharge conforms to the British Clean Air Act, the National Environment Management Agency (NEMA) Act or other relevant acts. .
1.1.4 POWER SUPPLY
The sub-contractor shall supply equipment which are suitable for running on a 415V, 3 phase, 50HZ or 240V, single phase, 50HZ electric power supply.
1.1.5 OIL STORAGE AND SUPPLY
The system shall consist of a bulk oil storage tank, daily tank, transfer hand fuel pump and associated pipe work. Oil from the bulk storage tank will be delivered to a high level daily tank situated in the incinerator room by use of a transfer hand pump and automatic electric pump.
1.1.6 SPARES AND MANUALS
The tenderer is to submit with his tender a list of recommended initial stock of spares together with their prices. A part from the burner spares mentioned here below, the spares prices are not to be included in the main summary of prices schedule but is to be separate and are meant to be ordered later if and when it becomes necessary and convenient to the client. The burner spares whose prices are to be included in the main summary of prices schedule (BQ) are:-
i) 1No. Set of safety controls
ii) 1No. Solenoid valve
iii) 1No. Oil ignition system
iv) 2No. Photo-electric cells
Two sets of operating and maintenance manuals (both for the incinerator and burners) must also be supplied. This include two sets of control schematic diagrams for all the controls and wiring.
1.1.7 BULK OIL STORAGE TANK
The bulk oil storage tank nominal capacity of 10,200 litres and complying with BS 799 part 5: 1975 shall be positioned on three concrete cradles.
The works shall include supply, delivery, assembling, erection, testing, commissioning and setting to work. The tank is to be of welded mild steel type with a design pressure of 40KN/m2 and storage temperature of 240 C. It is to be located adjacent to the incinerator and boiler house.
The tank shall be cylindrical with dished end and be constructed of 6mm thick block mild steel plates in accordance with BS 1966. Number one quality galvanised materials shall not be used.Welded construction parts shall be sprayed.
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The tank shall be pressure tested with a total head of water or equivalent, measured from the base of the tank, and equal to 1½ times the sum of:
(i) The height of the tank and
(ii) The design head above the top of the tank that is 3.5m of water.
The pressure shall be raised slowly and steadily until the specified test pressure is reached and that pressure shall be maintained for a period long enough to permit a thorough examination to be made to ensure that the tank is sound enough and shows no leaks or undue distortion. Welded joints shall be radiographed and a certificate issued. Should any defects be found, they shall be made good and the test procedure repeated until the tank is certified to be sound. The tests shall be carried out in the presence of the Engineer and subsequently, the sub-contractor will provide the Engineer with the test certificate.
The tank shall then be cleaned externally and provided with rust inhibiting primer before applying 2No. coats of bituminous paint. The inside shall also be cleaned and purged of any foreign matter before setting to work.
Ladders and platforms shall be thoroughly cleaned and freed from rust and scale and painted with a priming coat of approved paint.
The tank shall be provided with the following:-
(i) 450mm bolted inspection covers with liquid and vapour tight joint made with a gasket of fuel resistant materials.
(ii) 75mm (3”) vent socket screwed B-SP and pipe at the higher end of the tank with an unloading device to prevent the rise in tank pressure above the design pressure. The vent pipe shall be free from bends and shall have a continuous rise while being as short as convenient. It shall terminate in open air in a position where it cannot be tampered with. The open end shall be turned down and fitted with an open mesh wire cage.
(iii) 65mm diameter filling pipe with hose coupling connection
(iv) 50mm diameter gauging connection with lockable cap.
(v) 50mm diameter supply pipe
(vi) 25mm diameter water drain-off value
The tenderer shall supply hydrostatic oil contents gauge (level indicator) or a
properly calibrated stick (of dip tape) and access ladder to the top of the tank.
The filling pipe shall be extended inside the tank to within 150mm of tank bottom,
complete with anti-siphoning device.
The following information shall be permanently and clearly marked on the tank on the
centre line near the outlet connection.
• Gross capacity in litres
• Test pressure
• Date of test
• Maximum allowable working pressure
• Manufacturer’s name of trade mark
• Year of manufacture
• The number of British standard and type of tank
The tank shall be installed with a 25mm fall towards the water drain-off tapping point. The supply socket shall be extended inside the tank to prevent ingress of water in the supply line. The main contractor shall construct tank supports and bund walls to detail drawings produced by the sub-contractor. A valued drain off from the lowest part of the tank shall be provided complete with tail pipe and a provision for hose connection.
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1.1.8 TRANSFER HAND PUMP
A semi rotary hand pump shall be provided for filling the day storage tank from the oil drum. It shall be installed complete with all the necessary plumbing fittings and accessories.
1.1.9 DAILY SERVICE TANK
A daily storage tank of nominal capacity 1,800Litres shall be mounted at 2.5 metre high level in the incinerator room. Tank shall be manufactured from 6mm thick pressed steel plates of 1220mm x 1220mm black mild steel sheet, complete with bolted cover and adequate venting. The tank shall conform to BS 799 part 5 1995 and be provided with a contents sight tube. The tank shall be lagged with 50mm thick fibre glass insulation of 0.4W/m2 thermal conductivity and finished with 20SWG galvanized sheets cladding.
The tank shall be tested for any leaks of which if any is detected will be made good before the tank is painted externally with rust inhibiting paint. Tank to be securely bolted.
1.1.10 AUXILLIARY EQUIPMENT
All pipework used in the oil storage systems shall be to B.S. 1387 heavy grade. Joints shall be screwed, and sufficient unions must be provided to allow easy dismantling the equipment.
A 25mm diameter fire valve of the quick action lever operated dead weight type shall be installed, in the oil flow line. This shall be held in the open position by a light gauge steel cable attached to a fusible link. The fusible link shall be mounted directly over the burner. The warm burner oil feed pipe from the high level day tank shall be heated by an electric tracing tape properly wrapped around the pipe. The pipe shall then be insulated with 25mm thick fibre glass insulation and finished with gauge 22swg galvanized steel sheet.
The supply pipe from the bulk oil storage tank to the high level day has been installed by others but the tenderer shall allow for connection to the high level day tank. The tenderer shall also supply and install high capacity strainers along the supply pipe and the burner feed pipe.
1.1.11 PIPE SUPPORTS
The variety and type of supports shall be kept to a minimum and their design shall be such as to facilitate guide and secure fixing to match concrete masonry or wood.
Consideration shall be given when designing supports to the maintenance of desired pipe fall and the restraining of pipe movements to a longitudinal axial direction only.
The sub-contractor shall supply and install all steel work forming part of pipe support assemblies and shall be responsible for making good any damage to builders work associated with builders work installation.
Pipe runs shall be secured by clips connected to pipe hangers, wall brackets or trapeze type supports. ‘U’ bolts shall not be used for clips without prior approval of the Engineer.
The sub-contractor shall submit his entire proposal for the pipe supports to the Engineer for approval before any erection work commences.
1.1.12 ELECTRICAL WORKS
All wiring between items, plant and controls shall be executed by the tenderer. The tenderer shall provide adequate supervision to ensure that electrical connections are correctly made to all items of equipment and controls supplied by him, all to the Project Manager’s / Engineer’s satisfaction.
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1.1.13 INCINERATOR TESTING AND COMMISSIONING
The tenderer shall test and commission the incinerator in the presence of the Engineer.The tenderer shall also provide sufficient oil to last at least two (2) hours. The tenderer shall test and commission the incinerator in the presence of the Engineer and verify that the incinerator is functioning according to the specifications laid here-in and in the catalogues and manuals from the suppliers of he incinerator.The incinerator performance test shall be carried out in accordance to BS3316: part 4:1987.Should any defect be detected, it shall be rectified and the testing process repeated to the Project Manager’s satisfaction.
1.1.14 FIRE INSTRUCTION NOTICE
Proceed and procure and install as below;
Print fire instruction on the Perspex plate, 3mm thick with White Colour
Background measuring 510mm lengthx380mm width as follows;