Showing posts with label sludge. Show all posts
Showing posts with label sludge. Show all posts

Saturday, October 3, 2015

Oil room

Crude oil clarification

Objectives
1. Efficient separation of pure oil from crude oil.
2. Optimum recovery of pure oil at minimum oil loss.
3. Efficient separation & disposal of free water. 
4. Efficient separation of solid impurities & dissolved moisture.

The composition of crude oil
- A mixture of oil & water.
 * Non-dispersed oil in water – free oil.
 * Highly dispersed oil in water – mass under high pressure and oil is forced through the capillary ducts in the press cake – homogenized in watery medium.
- Oil in water emulsion – oil is highly dispersed in water with
       the present of emulsifiers.
- Water in oil emulsion – oil recovery is easy with temperature   

      between 80 – 100 degree Celsius.

Figure 1: The flow of oil and sludge in oil clarification

Process that need to be monitor
1. Oil content in Clarifier underflow, to monitor the efficiency of clarification process.
-should not exceed 8.0% ( wet basis).
2. Oil content in Centrifuge waste, to monitor final oil loss.
-should not exceed 0.75% & 1.5% (wet basis) respectively.
3. FFA, PV, moisture and dirt in production oil, to monitor production oil quality.
-dirt: should not exceed 0.02%.
-moisture: should be less than 0.20%.

Vibrating screen
The vibrating screen is a machine that functions as a filter that separates the oil and sludge from impurities, dirt and fibres that has not been separated by the sand trap. Vibrating screen are used before crude oil tank and before sludge tank. Before crude oil tank, the vibrating screen is used with the mesh size of 30 per inch. The vibrating screen before the sludge tank is using 40 per inch mesh size. The separated fibre, dirt and impurities will be returned to the digester to press out the oil. The oil and sludge will flow to crude oil tank.

Figure 2: vibrating screen    

Crude oil tank
Crude oil tank is a tank that functions to store raw oil before being transferred to the vertical clarifier. There are pumps that will pump up the oil from crude oil tank to vertical clarifier and the pump is triggered by a weight lever mechanism as when the oil in the crude oil tank reached a certain height, the pump will start running. Steam will be injected to keep the oil and sludge at 90 degree celcius to prevent the oil from solidify.
Vertical clarifier

The function of vertical clarifier is to separate pure oil and sludge and to minimize oil loss in sludge underflow. Vertical clarifier consists of a large vertical tank with a conical bottom. In the center of the tank is a large inlet pipe for the diluted crude oil (DCO). The oil builds up to a rather high depth of pure oil and leaves the tank continuously through an adjustable oil skimmer, usually a funnel of sufficient size. The sludge collects near the bottom of the tank and is flowing upward through a pipe. The discharge of underflow pipe is installed somewhat lower than the level of the adjusted oil skimmer. When no more DCO is fed to the tank, the discharge of oil and sludge will stop once oil layer equal sludge outlet layer. The oil layer will then be pressed upward and can be drained out preferably up to a foot of oil being left to prevent sludge water from being drained off. There is a pair of arm near the bottom part of the clarifier. The arm functions to stir the suldge that help to separate the oil particle that still stick to the sludge. The arm is stirring at slow rate. The Clarifier is also fitted with a steam heating coil in order to raise the temperature of the sludge and oil in the tank during the initial operation. Sand and other heavy impurities should be drained off periodically through the conical bottom of the Clarifier. The temperature of the clarification tank content is maintained at about 90 degree celcius to enhance oil separation.


Diluted Crude oil/FFB = Diluted crude oil / oil * Oil/FFB
= 263% * 21% = 55.26%
Average mill throughput: 85MT/hr
85MT/hr x 55.26% DCO= 46.971MT DCO/hr
Clarifier retention time: 2 hours
Clarifier capacity: 2 hr x 46.971 MT DCO/hr = 93.942MT DCO
Clarifier capacity is ~ 94MT

Figure 4: Vertical clarifier

Pure oil tank
Pure oil tank is a tank that used to store and heat up pure palm oil before being sent to the vacuum dryer. Pure oil tank is basically a reception and storage tank for the oil. Closed heating coil are normally installed in the tank to raise the temperature of the oil.

Vacuum dryer
Vacuum dryer functions to remove moisture from the crude palm oil. High moisture content of the purified oil will preclude a further set up of FFA content during storage and shipment. The oil must be further dried to a final moisture content of below 0.20% which is the final step in the oil recovery process. The oil will then being sent to oil storage tank and the process for the oil is finished. Every hour, the reading flow meter at of the oil will be recorded to know the amount of oil is being sent to storage tank. The water from vaccuum dryer will be flowing back to the hot water tank to be used as dilution water in press. 
Figure 6: vacuum dryer working principle

Oil storage tank

The dried oil is transferred to storage tank for storage prior to dispatch from the mill.
Since the rate of oxidation of the oil increases with the temperature of storage the oil is normally maintained around 50°C, using steam-heating coils, to prevent solidification and fractionation. Iron contamination from the storage tank may occur if the tank is not lined with a suitable protective coating.


Sludge tank
Sludge tank is reception and storage for the sludge with some oil before send to desander. The sludge from the vertical clarifier will be send to vibrating screen to remove the dirt and fibre and then goes to sludge tank. Live steam will be injected in the sludge tank to prevent the sludge from clogging. The The sludge will then being sent to desander afterwards. There is an opening below the sludge tank. The opening is used to clean out the sand deposition on the bottom of the sludge tank.

Desander
Desander’s function is to remove the sand contained in the sludge prior to centrifugal separation. The desander consists of a pump and a stainless steel cyclone which has a waste receiver connected below it. The sludge contain a significant amount of fine sand. If it is not removed, it will cause the nozzle in centrifuge stork to rapid abrasive wear. Sludge is pumped to the desanding cyclone and is admitted tangentially. Centrifugal force set up in the cyclone will cause the heavy sand particles to move towards the wall of the cyclone and then flow into the waste receiver. The lighter phase move through the primary vortex in the middle of the cyclone out to the next stage. 2 bar differential pressure between inlet and outlet must be achieved. There is a timer in the system to set the time to empty the waste receiver every 15 minute.
The desander station in this mill is double stage desanding system. The sludge will flow through the 1st stage desander, some of the sand are removed. The sludge will then pump to the tank and flow to 2nd stage desander to remove the excess sand. The sludge flow back to the tank and then will be pump to feeding tank before go to stork centrifuge. The sand will be sent to a vibrating screen to filter out the sludge that being washed out with the sand. The sludge will be recycle back to the sludge tank. 
Figure : desander working principle

Figure: Double stage desander                                

Stork centrifuge
Stork centrifuge function to separate the oil from the sludge to recover the oil losses in the sludge without affecting the throughput of the mill. There are a total number of 16 stork centrifuge in the mill. The capacity of the stork centrifuge is 3.5 mt/hr. The stork centrifuge consists of a casing divided between top and bottom half, with an inspection cover on the top section to permit access to the nozzles. The bowl housing consists of two disc-shaped sections of cast iron which together with the wearing strips, form the protective casing to the cast iron material external casing. The rotor which is constructed entirely from s/steel is in the shape of a star and at the end of each fin or tip is fitted a nozzle holder which holds a nozzle with sizes of 1.7mm. The non-oily sludge water is jetted through the nozzle. In operation, the sludge oil tank is fed by gravity flow from the sludge feed tank.
The machine is normally rotated at 1400 rpm. Due to centrifugal force, the heavier particles of dirt and water are forced to the extreme end of the rotor and passed out through the nozzles and discharged off. The pure oil being lighter in comparison builds up in the center of the bowl and discharged through the oil recovery stainless steel pipe. The oil is then flow to crude oil tank.

Figure : Stork centrifuge internal view 


Thresher and EFB press

Threshing objectives

1. Separate the sterilised fruits from sterilised bunch stalks by beating the fruit.
2. Maintain the oil looses and kernel losses at below the recommended level. 
3. Provide a well distributed beating area on the fruit. 



Principle of Drum Stripper

The machine consists of a long horizontal cylindrical drum which is rotating. The sterilised bunch are fed in continuously at one end and stalks pass out continuously at the other end. The surface of the drum is made up of tee-bars running parallel to the axis of the cylinder and spaced far enough apart to permit the escape of fruit and wouldn’t let the stalk from passing out between them.

The rate of rotation can be calculated with the formula below.

 n = 40 x sqrt((D-d)/2)/(D-d)

n = rpm
D = thresher diameter
D = fruit bunch diameter

The rpm of the drum need to be in the value that the bunches of normal size are lifted by centrifugal action, assisted by lifting bars fitted to the inside of the drum.The lifting bars are arranged in the way that slanted to let the bunch flow to the outward direction each it fall. Once the bunches reach the top of the drum, then they will fall freely, passing approximately through the axis of the drum and strike the bottom with sufficient force to dislodge much of the fruit. The fruit passes out between the tee-bars and fall into a screw conveyor. The bunch is then lifted up and fall again, this process repeated to the numbers of times that all the fruits are remove from the bunch and the stalk gradually move to the end of the drum and drops out. 
Figure 1: First drum thresher’s lift bar position

Figure 2: Second drum thresher’s lift bar position

Auto Feeder



The bunch feeder is where the sterilised bunch will be drop into from the cages by the crane. In the auto feeder, the bunches will be moving into the thresher by chain. Bunch feeder is to allow the bunches to be move continuously and dropped at a constant rate into the thresher so that the thresher wouldn’t be overloaded. This can prevent the lifting bar and the shaft from being broken easily and increase the effectiveness of threshing process. By using bunch feeder, we are able to set the amount of bunches and its rate of dropping by changing the rpm of the feeder chain. 


Figure 3: Autofeeder loaded with sterilised bunches


Operation of Hoist
Hoist crane is the mechanism to lift the cages and pour the sterilised bunches to the bunch feeder. The hoist is controlled by manual. There are 2 axis directional control and 1 for rolling the cage over to drop the bunches in the cages. 
There are 3 hoist in this mill. All of them are rated with 6 tonnes maximum load. One of the crane has rated power of 17.8kw and 20kw for the other 2.

Main part of Hoist
1.     Chain sprocket dan Rotary chain (tilt-up dan tilt-down)
2.     Hook frame 
3.     Wire rope 
4.     Wire drum
5.     Traveling motor/gear box
6.     Tilt up-tilt down motor/gear box
7.     I – Beam (trail for travelling forward and backward)
8.     Coil Spring cable
9.     Wire rope pulley

Crane action:

Time (seconds):
Locating the chain on the cage
15
Lifting the cage to the autofeeder
65
Rotating the cage to pour the bunches
25
Lower the cage and release on the trail
55
total

Figure 5: Operation of hoist crane 

Safety feature of the Hoist crane

The are brake system in the crane. When the operator is not moving or release the control stick, the crane will stop at the position. This ensure that the crane would not easily out of control due to human error. 
Beside that, when operating the crane, it should be slow especially when lifting the cage off the ground. When lifting the cage that is far from the threshing station, the cage should be lifted in the way that it goes toward the the station in low height then only lift up to the autofeeder. If the cage is swinging, the operator should put the cage down to the ground first, make sure it is stable and lift it up again. Every morning, there will be checking on the cages to make sure the cages are in good condition as it won’t slip when the chain is holding the cage. The cages that are broken or needed maintenance, it will be put at the side to be repair. 

Conveyor
There are a few type of conveyor used in this mill. Conveyor is used to transport the medium such as fruit, EFB, kernel, shell or fibre produced from EFB from one location to another, even on different level. Conveyor systems allow quick and efficient transportation for different type of materials. It greatly reduce the need of human labour. 

Scrapper conveyor:
Made up of bar, roller, bushings, sidebars and pins. The chains is moving the bars and the bars will push the medium it carry.
Figure 6: Component of chain on conveyor

Screw conveyor:
A screw conveyor is a mechanism that uses a rotating helical screw blade, within a tube, It is used to transport the fruits in this mill. They are used in horizontal or incline way.

Hard Bunch & USB

Hard Bunch is the bunch that have most of the fruit (80%) still attached to the bunch and the unstripped bunch (USB) is the bunch that contain 30% of the fruit on the bunch after threshing. The stalks which still have fruits attached even after they passed through the stripper are hard bunches or unstripped bunches(USB). The reason for the fruit remaining in the stalk is inadequate sterilisation. The sterilisation conditions are chosen based on the condition of the majority of the bunches. So some bunches which are under ripe or abnormal in some other way may require long sterilising time than average to allow them to strip completely. The amount of hard bunch is tolerated at below 3%. There will be one worker checking at the bunches that is threshed to find out the bunches that are no fully stripped. The unstripped bunches will be throw back to the cage and to be resterilised. The grading of the hard bunch and USB will be 2 hours interval and 100 sample will be checked. 

Figure 7: Hard bunch

Figure 8: USB

EFB press

During threshing and sterilizing, they will be a certain amount of oil being absorbed by the calyx leaves and the stalk. The loss of oil absorbed can be affected by the sterilising condition and stripper. Prolonged sterilising will increase oil loss and the delay between sterilising and stripping will give extra time for oil to be absorbed. The purpose of EFB press is to reclaim the oil by squeezing the EFB. This increase amount of oil produce by ensuring that every last bit of oil is being extracted from the EFB and nothing goes to waste. This is a very important process as it will increase the OER of the mill. 

Figure 9: Top layout view of thresher and EFB press station
Discussion
Hard bunch USB:
There amount of hard bunch and USB after threshing appeared to be differ for each batch of sterilised bunches based on my observation.This means that sterilising condition greatly influence the result of the sterilised bunches. To reduce the amount of bar bunch and USB, sterilise condition must be well controlled at optimize condition.
Besides, design of thresher drum also affected the number of USB and hard bunch produced. The table below is the result taken from 200 samples of each of the thresher at 4.15pm 21th July 2015. The bunches are from steriliser number 4.

2nd thresher
3rd thresher
USB
Hard bunch
USB
Hard bunch
11
3
8
3

Both of the threshers are having different desgin on the drum. This show that the drum design for the threshers influence that result of USB and Hard bunch produced. The 2nd thresher show the amount of both USB and Hard bunch produced is more the the 3rd thresher. So the 3rd thresher’s dru m design appeared to be more effective in stipping the bunches.


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