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Industri Miyak Kelapa Sawit | Palm Oil Industri Overview

Posted by Flora Sawita Labels: Agro-industry, budidaya sawit, industri sawit, Perkebunan

INDUSTRI MINYAK KELAPA SAWIT

I. Minyak Kelapa Sawit

Produk minyak kelapa sawit sebagai bahan makanan mempunyai dua aspek kualitas. Aspek pertama berhubungan dengan kadar dan kualitas asam lemak, kelembaban dan kadar kotoran. Aspek kedua berhubungan dengan rasa, aroma dan kejernihan serta kemurnian produk. Kelapa sawit bermutu prima (SQ, Special Quality) mengandung asam lemak (FFA, Free Fatty Acid) tidak lebih dari 2 % pada saat pengapalan. Kualitas standar minyak kelapa sawit mengandung tidak lebih dari 5 % FFA. Setelah pengolahan, kelapa sawit bermutu akan menghasilkan rendemen minyak 22,1 % ‐ 22,2 % (tertinggi) dan kadar asam lemak bebas 1,7 % ‐ 2,1 % (terendah).

II. Standar Mutu Mnyak Kelapa Sawit

Mutu minyak kelapa sawit dapat dibedakan menjadi dua arti, pertama, benar‐benar murni dan tidak bercampur dengan minyak nabati lain. Mutu minyak kelapa sawit tersebut dapat ditentukan dengan menilai sifat‐sifat fisiknya, yaitu dengan mengukur titik lebur angka penyabunan dan bilangan yodium. Kedua, pengertian mutu sawit berdasarkan ukuran. Dalam hal ini syarat mutu diukur berdasarkan spesifikasi standar mutu internasional yang meliputi kadar ALB, air, kotoran, logam besi, logam tembaga, peroksida, dan ukuran pemucatan. Kebutuhan mutu minyak kelapa sawit yang digunakan sebagai bahan baku industri pangan dan non pangan masing‐masing berbeda. Oleh karena itu keaslian, kemurnian, kesegaran, maupun aspek higienisnya harus lebih Diperhatikan. Rendahnya mutu minyak kelapa sawit sangat ditentukan oleh banyak faktor. Faktor‐faktor tersebut dapat langsung dari sifat induk pohonnya, penanganan pascapanen, atau kesalahan selama pemrosesan dan pengangkutan.

Dari beberapa faktor yang berkaitan dengan standar mutu minyak sawit tersebut, didapat hasil dari pengolahan kelapa sawit, seperti di bawah ini :

a. Crude Palm Oil

b. Crude Palm Stearin

c. RBD Palm Oil

d. RBD Olein

e. RBD Stearin

f. Palm Kernel Oil

g. Palm Kernel Fatty Acid

h. Palm Kernel

i. Palm Kernel Expeller (PKE)

j. Palm Cooking Oil

k. Refined Palm Oil (RPO)

l. Refined Bleached Deodorised Olein (ROL)

m. Refined Bleached Deodorised Stearin (RPS)

n. Palm Kernel Pellet

o. Palm Kernel Shell Charcoal

Syarat mutu inti kelapa sawit adalah sebagai berikut:

a. Kadar minyak minimum (%): 48; cara pengujian SP‐SMP‐13‐1975

b. Kadar air maksimum (%):8,5 ; cara pengujian SP‐SMP‐7‐1975

c. Kontaminasi maksimum (%):4,0; cara pengujian SP‐SMP‐31‐19975

d. Kadar inti pecah maksimum (%):15; cara pengujian SP‐SMP‐31‐1975

III. Komposisi Kimia Minyak Kelapa Sawit

Minyak kelapa sawit dan inti minyak kelapa sawit merupakan susunan dari fatty acids, esterified, serta glycerol yang masih banyak lemaknya. Didalam keduanya tinggi serta penuh akan fatty acids, antara 50% dan 80% dari masing‐masingnya. Minyak kelapa sawit mempunyai 16 nama carbon yang penuh asam lemak palmitic acid berdasarkan dalam minyak kelapa minyak kelapa sawit sebagian besar berisikan lauric acid. Minyak kelapa sawit sebagian besarnya tumbuh berasal alamiah untuk tocotrienol, bagian dari vitamin E. Minyak kelapa sawit didalamnya banyak mengandung vitamin K dan magnesium.

Ukuran dari asam lemak (Fas) dalam minyak kelapa sawit sebagai acuan:

a. Kadar Asam Lemak Dalam Minyak Sawit

· Palmitic C16 �� 44.3%

· Stearic C18 �� 4.6%

· Myristic C14 �� 1.0%

· Oleic C18 �� 38.7%

· Linoleic C18 �� 10.5%

· Lainnya �� 0.9%

b. Asam Lemak Dalam Minyak Inti Sawit

· Lauric C12 48.2%

· Myristic C14 16.2%

· Palmitic C16 8.4%

· Capric C10 3.4%

· Caprylic C8 3.3%

· Stearic C18 2.5%

· Oleic C18 15.3%

· Linoleic C18 2.3%

Standar Mutu Minyak Goreng Berdasarkan SNI - 3741- 1995

Kriteria Persyaratan

1. Bau dan Rasa Normal

2. Warna Muda Jernih

3. Kadar Air max 0,3%

4. Berat Jenis 0,900 g/liter

5. Asam lemak bebas Max 0,3%

6. Bilangan Peroksida Max 2 Meg/Kg

7. Bilangan Iod 45 – 46

8. Bilangan Penyabunan 196 – 206

9. Index Bias 1,448 - 1,450

10. Cemaran Logam Max 0,1 mg/kg

IV. Perbandingan antara Minyak Filma, Bimoli dan Minyak Curah

1. Minyak Filma

Minyak filma ini mengandung 3 Nutrisi di dalamnya yaitu : Omega 6 Omega 9 Vitamin E. Filma mengandung asam lemak tak jenuh, Omega 9 dan Omega 6. Asam lemak tak jenuh dapat membantu menjaga kadar kolesterol sebagaimana adanya. Omega 6 adalah asam lemak esensial yang diperlukan tubuh.Filma berwarna kuning keemasan berasal dari kandungan Beta Karoten alami (Pro Vitamin A).Filma diproses dari buah sawit segar pilihan dengan Sistem Pemurnian Terintegrasi Penuh sehingga menghasilkan minyak goreng berkualitas jernih bernutrisi

Gambar 2. minyak goreng Filma Yang siap untuk dikonsumsi

2. Minyak Bimoli

Beberapa keunggulan minyak Bimoli diantaranya :

o Mengandung Omega 9 (sekitar 40-45%) dan Omega 3 cis.

o Bebas kolesterol.

o Proses produksi yang digunakan adalah Pemurnian Multi Proses (PMP) yang meliputi 6 tahap pemurnian

o Aman untuk dikonsumsi.

o Penyusunan maksimum adalah lima karton. Jauhkan dari panas dan sinar matahari. Dapat disimpan selama 24 bulan.

Gambar 3. minyak bimoli yang siap untuk dikonsumsi

3. Minyak Curah

Minyak goreng curah berbeda dengan minyak goreng bermerek, seperti filma, bimoli dan sebagainya. Karena minyak goreng bermerek dua kali penyaringan, sedangkan minyak goreng curah proses penyaringan hanya satu kali,'' terangnya. Sehingga dari warnanya berbeda dengan minyak goreng bermerek yang lebih jernih dibanding minyak goreng curah. Begitu juga kandungan yang terdapat antara minyak curah dan minyak kemasan. Dari segi kandungan minyak curah kadar lemaknya lebih tinggi dan juga kandungan asam oleat dibanding minyak kemasan,'' tuturnya. Namun tidak ada masalah menggunakan minyak curah, asalkan tidak berlebihan dan tidak digunakan berulang-ulang kali, sampai berwarna coklat pekat hingga kehitam-hitaman. Karena pemakaian berulang-ulang pada minyak makan, sangat tidak baik bagi kesehatan. Sekedar diketahui, minyak curah hanya mengalami penyaringan sampai tahap olein. Dan masih mengandung soft stearin (minyak fraksi padat) pada tingkat tertentu. Oleh karena itu minyak curah biasanya lebih keruh dibandingkan minyak bermerek. Selain itu tingkat sanitasi dan kebersihannya kurang baik, tidak sebersih minyak bermerek. Oleh karena itu, kalau ada minyak curah yang bening dan bersih sebenarnya lebih aman karena tidak mengandung antioksidan. Tetapi jenis itu jarang dijumpai di pasar.

Gambar 4. Minyak Curah

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Palm Oil Milling Process

Posted by Flora Sawita Labels: CPO, crude palm oil, Crude Palm Oil (CPO) and Palm Kernel Oil (PKO), crude palm oil industry, industri sawit, mill, palm oil mill, plam oil, Processing Plant, Proses

Edible Oil Processing - Production

PALM OIL MILLING PROCESS

Introduction

Palm oil is extracted from fresh fruit bunches (FFB) by mechanical process, where a mill commonly handles 60 to 100mt per hour of FFB. The modern palm oil mill of today is based predominantly on concepts developed in the early 50s (Mongana Report). An average size FFB weighs about 20-30kg and contains 1500-2000 fruits (Figure1). The FFBs are harvested according to harvesting cycles, and delivered to the mills on the same day. The quality of crude palm oil is dependent on the care taken after harvesting, particularly on the handling of the FFBs.

Figure 1. Fresh fruit bunches waiting for processing at palm oil mill

A palm oil mill produces crude palm oil and kernels, as primary products and biomass as secondary product. The capacity of mills varies between 60- 100 tons FFB/h. A typical mill has many operation units as shown in Figure 2. This comprises of sterilization, stripping, digestion and pressing, clarification, purification, drying and storage. For the kernel line, there are steps such as nut/fibre separation, nut conditioning and cracking, cracked mixture separation, and kernel drying, storage. The dried kernels are often sold to palm kernel crushers for extraction of crude palm kernel oil. In some integrated plants, kernel crushing facilities exist side by side at the same complex.

Figure 2. Flow chart for the palm oil process (from Sivasothy, 2000).

Sterilisation

This first step in the process is crucial to the final oil quality as well as the strippability of fruits. Sterilization inactivates the lipases in the fruits, and prevents build-up of free fatty acids (FFA). In addition, steam sterilization of the FFBs facilitates fruits being stripped from the bunches. It also softens the fruit mesocarp for digestion and release of oil, and conditioning of nuts to minimize kernel breakage. Air is removed from the sterilizer by sweeping in steam in single-peak, double-peak or triple-peak cycles. In general, bunches are cooked using steam at 40psig. in horizontal cylindrical autoclaves for 60-90 minutes. The length of the sterilizer is dependent on the number of cages required for operation of the mill. Each cage can hold 2.5 to 10tons of FFB. Steam consumption varies from 140 kg/ton FFB for a single-peak cycle to 224 kg/ton FFB for a triple – peak cycle (Sivasothy et al.1986). Inadequate sterilzation affects the subsequent milling processing stages adversely.

In recent years, new technology on sterilization saw the introduction of continuous sterilizers. Sivasothy’s (2006) continuous sterilizer showed improved fruit strippability, even with usage of low pressure steam or atmospheric steam. The new system consists of conveyor belt taking crushed FFBs into the continuous sterilizer, where the fruits are sterilized and subsequently discharged. This reduces much of the machinery associated with conventional sterilizers. In addition, there are cost savings in terms of manpower requirements, and maintenance.

Vertical sterilizers are also available, which are much cleaner and easier to operate than conventional sterilizers.

Another type of sterilizer technology, the Tilting sterilizer (Loh, 2010) also eliminates much of the machinery associated with conventional sterilizers. The technology is the latest design that offers improved milling efficiency, and reduced labour and maintenance cost.

Figure 3. A conventional sterilizer

Stripping

Stripping or threshing involves separating the sterilized fruits from the bunch stalks. Sterilized FFBs are fed into a drum stripper and the drum is rotated, causing the fruits to be detached from the bunch. The bunch stalks are removed as they do not contain any oil. It is important to ensure that oil loss in the bunch stalk is kept to a minimum. The stalks are often disposed by incineration, giving ash as potash fertilizer, and fuel for boilers. Others are transported to the plantations for use as fertilisers in mulching near the palms. The total oil loss absorbed on the stalks depends on the sterilizing conditions and partly on the way the stripper is operated. Prolonged sterilization will increase oil loss in stalks. Irregular feeding of the stripper may also result in increase of oil loss in stalks. Stalks which have fruits still attached on them are called hard bunches, and have to be recycled back to sterilizers for further cooking. Hard bunches are detected by visible inspection.

Digestion and Pressing

After stripping, the fruits are moved into a digester where, the fruits are reheated to loosen the pericarp. The steam heated vessels have rotating shafts to which are attached stirring arms. The fruits are rotated about, causing the loosening of the pericarps from the nuts. The digester is kept full and as the digested fruit is drawn out, freshly stripped fruits are brought in. The fruits are passed into a screw press, where the mixture of oil, water, press cake or fibre and nuts are discharged. Improvements in press designs have allowed fruits to undergo single or multiple pressing. Second stage pressing on the press cake fibres enables more oil to be extracted.

Clarification

A mixture of oil, water, solids from the bunch fibres is delivered from the press to a clarification tank. In the conventional process, separation of the oil from the rest of the liquor is achieved by setting tanks based on gravity. The mixture containing the crude oil is diluted with hot water to reduce its viscosity.A vibrating screen helps remove some of the solids. The oil mixture is heated to 85-90◦C and allowed to separate in the clarification tank. A settling time of 1-3 h. is acceptable. Oil from the top is skimmed off and purified in the centrifuge prior to drying in vacuum dryer. The final crude palm oil is then cooled and stored. The lower layer from the clarification tank is sent to the centrifugal separator where the remaining oil is recovered. The oil is dried in vacuum dryers, cooled and sent to storage tanks.

Decanters

Decanters are also used in some mills as an alternative to separating the suspended solids from crude palm oil in a clarification tank. Various design of decanters are available. Their usage is however, hampered by higher maintenance costs from the wear and tear. An advantage to the use is the reduction in palm oil mill effluent. Sulong and Tan (1996) had proposed a membrane filter press for oil and solids recovery. The cake is discharged as solid waste for fertilizer production or animal feed, while the oil is recovered.

Oil Losses during Processing

Oil losses in mills vary from mill to mill, and much attention is given to the control of oil loss. The main oil loss are from sterilizer condensate, empty bunches, fruit loss in unstrapped bunches, press cake fibre, nuts and sludge. Over-ripe bunches will lose more oil during sterilization. To minimize this, shorter sterilizer cycles are used, or better control of bunch ripeness and quality will help ensure less wastage. A typical oil loss in sterilizer is estimated to be 0.1% to FFB. Oils recovered from sterilizer condensate should be used as technical oils, as they often contain higher iron content and would reduce oil stability if mixed with the crude production oil.

Kernel Production

The press cake from the digester is fed to a vertical column (depericarper) where air is channeled to lift the fibre, thus separating the fibre from the nuts. The nuts are passed to a polishing drum at the bottom of the depericarper, where pieces of stalks are removed. A nutcracker cracks the nuts after the conditioning and drying process. A ripple mill is also used instead of nut cracker. The mixture of cracked nuts and shells are separated via a winnowing system, followed by a hydrocyclone or a clay bath. A hydrocyclone uses centrifugal force to separate the kernel from the shell using water. The clay bath principle works on the specific gravity of kernel of 1.07 and the shell of 1.17. The kernels will float while the shells sink in a clay bath mixture of SG 1.12. The kernels are then dried in hot air silos to moisture content of less than 7%. About 0.4mt of kernels are produced with every mt of CPO.

Biomass

The amount of solid palm oil waste available from a mill can be substantial. This consists of empty fruit bunches (EFB), palm kernel shell, mesocarp fibres, and possibly solids from decanters. In most cases, this biomass especially, the EFB, palm kernel shell and mesocarp fibres are used as fuel in the mill, generating enough electricity for running the mill. Besides usage as fuel, the biomass together with fronds and trunks can be left in the fields as fertilizers. EFBs can also be combined with polyurethane ester (PU) to prepare medium density fibreboard, giving higher impact strength and better water resistance (Khairiah, 2006).

Type of biomass	Average calorific value(kcal/kg)	Range (kcal/kg)
Table 1. Dry basis calorific value of palm waste materials (Source: Yap, 2010).

Empty fruit bunches	18795	18000-19920
Fibre	19055	18800-19580
Palm kernel shell	18884	18880-18895
Nut	24481	24256-24830

Treatment of Raw Palm Oil Mill Effluent (POME)

A palm oil mill produces an average of 0.65 tonne of raw palm oil mill effluent (POME) from every ton of FFB processed. POME is the main cause of environmental pollution due to its high acidity, high biological demand (BOD) and chemical oxygen demand (COD). Conventionally, anaerobic digestions in ponding systems or aerobic treatments are able to bring the BOD levels to below 100 mg L^-1. Open steel tank digesters are used for tapping the biogas for power consumption. In Malaysia, certain areas have more stringent requirements (BOD of less than 20mg L^-1. Tertiary systems have been developed as new systems to provide effluent treatment in a more sustainable manner, as well as achieving the standards required by regulatory bodies. These include biological sequencing batch reactors, bio-filtration systems, systems with high aeration rates, activated sludge plants with aerobic reactors, bio-flow polishing plants, as well as membrane bioreactors. More palm oil plantations are investing into these technologies to harvest the biogas for fuel, and re-use other biomass materials for fertilizers, bio-composite materials, etc.

References

Khairiah, B and Khairul, A.M.A. Bio composites from oil palm resources. Journal of Oil Palm Research, April, 103-113 (2006).
Loh, T.K. Tilting sterilizer. In: Palm Oil Engineering Bulletin, No 94, pp. 29-42 (2010). MONGANA Report, Volume 1 and 2 Coopérative des Producteurs et exportateurs de l’huile de palme du Congo Belge. (1955).
Sivasothy, K., Shafil, A.F. and Lim, N.B.H. Analysis of the steam consumption during sterilization., Workshop on recent developments in palm oil milling technology and pollution control, Kuala Lumpur, p. 19, Malaysian Palm Oil Board, Kuala Lumpur )(1986).
Sivasothy, K. Advances in Oil Palm Research, Vol 1, 747, Y. Basiron, B.S. Jalani, and K.W. Chan (eds) , Malaysian Palm Oil Board, Kuala Lumpur) (2000).
Sivasothy, K. Continuous sterilization: the new paradigm for modernizing palm oil milling. Journal of Oil Palm Research, April, 144-152 (2006).
Sulong, M. and Tan, R.C.W. Filtration system for crude palm oil clarification and purification. In: Proc. Of the 1996 PORIM International Palm Oil Congress, Kuala Lumpur, pp. 410-424. (B. Muhamd, A.N. Ma, M.S. Affandi, Y.M. Choo, A. Kuntom, C.L. Chong, A.G.M. Top, K. Yaakob, S. Ahmad, J. Thambirajah, Z.A.A. Hassan and R. Masri (eds), Malaysian Palm Oil Board, Kuala Lumpur)(1996).
Yap, A.K.C. Palm waste as alternative fuel for cement plant. Palm Oil Engineering Bulletin No 91, 13-21 (2010).

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Asian Agri Group | Alamat Asian Agri | Asian Agri Medan | Jakarta

Posted by Flora Sawita Labels: industri sawit, Perkebunan, plam oil, RSPO, SAWIT

Logo Asian Agri Group

Asian Agri Group adalah group perusahan kelapa sawit kelas dunia yang berbasis di Indonesia. Asian Agri juga merupakan perusahaan terkebunan yang terbesar di Indonesia. Sampai saat ini asian agri melelola lebih dari 100.000 Hektar di Pulau Sumatera dan bermitra plasma dengan petani dengan luas 60.000 Hektar

Asian Agri Group percaya produksi dan penggunaan minyak sawit harus di lakukan secara berkelanjutan berdasarkan pertimbangan ekonomi, social dan lingkungan maka dari itu PT. Inti Indosawit Subur, salah satu perusahaan unggulan dari Group Asian Agri, terlah menjabat sebagai anggota Roundtable on Sustainable Palm Oil (RSPO) sebagai sebuah global multi-stakeholder yang ber inisiatif untuk mendorong pertumbuhan dan penggunaan minyak sawit yang berkelanjutan.

Adapun Alamat Asian Agri Group ialah sebagai berikut :

Asian Agri Group . Perusahaan bidang usaha Minyak Kelapa Sawit / Palm oil
Uniplaza Building, 6th Floor, Jl. Letjen. MT. Haryono No. A-1
Medan 20231
Telp. (061) 4532155, Telp. (061) 4532388, Telp. (061) 4532532
Fax. (061) 4532095

Asian Agri Group (Perwakilan Jakarta) .
Perusahaan bidang usaha Minyak Kelapa Sawit / Palm oil
Jl. MH. Thamrin No. 31
Jakarta Pusat 10230
Telp. (021) 23586611
Fax. (021) 23586620

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Dalam Dua Bulan, Astra Jual 201.753 Ton Sawit

Posted by Flora Sawita Labels: Industri Kelapa Sawit, industri sawit, Perkebunan, trade

Jakarta - Grup Astra melalui anak usahanya, PT Astra Agro Lestari Tbk (AALI) mencatat kenaikan 15% atas penjualan minyak sawit mentah alias crude palm oil (CPO) 201.753 ton

Berdasarkan rilis yang dipublikasikan, Selasa (27/3/2012), penjualan CPO sampai Februari 2012 naik dari periode sebelumnya 175.390 ton. Penjualan domestik masih dominan, dengan angka 190.253 ton. Sementara ekspor hanya 11.500 ton.

Volume penjualan CPO dalam negeri tumbuh 16,5% dari periode sebelumnya 163.302 ton. Sedangkan CPO ekspor turun 4,9% dari sebelumnya 12.088 ton. Sementara volume jual kernel pun tumbuh 91,9% menjadi 40.154 ton dari periode sebelumnya 20.922 ton.

"Namun untuk harga jual rata-rata baik CPO maupun kernel mengalami penurunan masing-masing 12,4% dam 38,5%," kata Investor Relation ALLI, Rudy Limardjo.

Ia menambahkan, produksi CPO dunia tahun 2012 berdasarkan data oil price diprediksi mencapai 52,37 juta ton. Produksi naik 4,3% dari sebelumnya 50,23 juta ton.

Kenaikan disebabkan adanya penetrasi lahan menghasilkan sebesar 4,6% menjadi 14,06 juta ha. Sementara, tahun 2011 produksi CPO dunia naik 9,5%. Produksi ditopang oleh dua negara, Indonesia 23,9 juta ton dan Malaysia 18,91 juta ton.

(wep/ang)

http://finance.detik.com/read/2012/03/27/123245/1877521/1036/dalam-dua-bulan-astra-jual-201753-ton-sawit

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Penjualan Komoditas Perkebunan Naik, JAWA Cetak Laba Rp 185 miliar

Posted by Flora Sawita Labels: Agro-industry, budidaya sawit, Industri Kelapa Sawit, industri sawit, Perkebunan

Jakarta - PT Jaya Agra Wattie Tbk (JAWA) emiten sektor perkebunan mencatat laba bersih tahun buku 2011 Rp 185,42 miliar naik 84,13% dari periode sebelumnya Rp 100,7 miliar. Namun laba bersih per saham turun dari Rp 52 per lembar menjadi Rp 64 per lembar.

Naiknya laba ditopang oleh pertumbuhan penjualan komoditi karet sawit, kopi, teh dan lain-lain. Penjualan bersih perseroan mencapai Rp 647,059 miliar naik dari sebelumnya Rp 413,43 miliar.

Nerdasarkan laporan keuangan JAWA yang dipublikasikan, Selasa (27/3/2012), penjualan ekspor hasil kebun perseroan mencapai Rp 82,73 miliar. Terdiri dari ekspor karet dan kopi masing-masing Rp 81,91 miliar dan Rp 820,95 miliar. Tahun lalu ekspor perseroan hanya ditopang oleh komoditi kopi Rp 33,59 miliar.

Penjualan dalam negeri karet dan lain-lain meningkat dari Rp 379,83 miliar menjadi Rp 564,32 miliar. Laba kotor JAWA pun mencapai Rp 302,41 miliar usai terpangkas beban penjualan Rp 344,64 miliar. Laba kotor tahun lalu hanya Rp 182,26 miliar.

Laba sebelum pajak juga meningkat Rp 111,17 miliar dari Rp 135,27 miliar menjadi Rp 246,39 miliar. Laba bersih akhirnya parkir pada level Rp 185,42 miliar dari sebelumnya Rp 100,7 miliar.

Total aset JAWA hingga 31 Desember 2011 mencapai Rp 1,94 triliun, naik dari sebelumnya Rp 1,04 triliun. Sementara total kewajiban naik dari Rp 658,2 miliar menjadi Rp 807 miliar.

(wep/ang)

http://finance.detik.com/read/2012/03/27/112627/1877403/6/penjualan-komoditas-perkebunan-naik-jawa-cetak-laba-rp-185-miliar

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Menteri BUMN Dahlan Iskan | Manfaatkan Perkebunan Sawit dalam Meningkatkan Produksi Sapi

Posted by Flora Sawita Labels: industri sawit, Perkebunan, sapi

Mentri BUMN Dahlan Iskan

Yogyakarta - Menteri BUMN Dahlan Iskan mengaku prihatin setiap tahunnya RI harus impor sapi 350.000 ekor. Namun Dahlan tak hanya di bibir saja mengatakan prihatin, Ia mempunyai strategi khusus untuk mendongkrak produksi sapi dalam negeri. Apa strategi tersebut?

Dengan memanfaatkan PT Perkebunan Nusantara (PTPN) I - XIV, Dahlan memiliki ide meningkatkan produksi sapi di lahan kelapa sawit dimiliki BUMN perkebunan tersebut.

"Lahan untuk kelapa sawit bisa dilakukan perluasan usaha, dengan memelihara sapi potong," kata Dahlan di sela acara talkshow "Pemimpin Muda Belajar Merawat Indonesia di Gedung Pusat Kebudayaan UGM, Yogyakarta, Kamis (29/3/2012).

"Saya prihatin impor sapi itu mencapai 350 ribu ekor per tahun sementara itu Indonesia berpotensi menjadi peternak yang besar," ungkapnya.

Dijelaskan Dahlan secara singkat, cara meningkatkan produksi dalam negeri sapi potong ini dengan mengembangkan perkebunan sawit yang diwajibkan nantinya ikut memelihara sapi. Nantinya untuk tahun 2012-2013 bisa ditargetkan 100 ribu ekor.

"Kemudian tahun berikutnya pelan-pelan sampai 350 ribu ekor," kata Dahlan.

"Di Indonesia ini terutama di Sumatera beberapa PTPN mengelola perkebunan yang sudah ikut memelihara sapi, contohnya PTPN VI di Jambi sudah memelihara 10 ribu ekor. Kemudian PTPN lain juga sampai 15 ribu," imbuh Dahlan.

Menurut Dahlan, dalam mengembangkan sapi ini PTPN tidak perlu khawatir terkait dengan ketersediaan pakan. Karena, sambung Dahlan di kebun kelapa sawit, pelapah pohon sapi itu jika digiling halus bisa jadi makanan.

"Jadi itu tidak perlu lagi beli pakan. Saya kira realisasi ternak sapi di kebun sawit harus dilakukan tindakan bukan lagi dengan seminar atau dialog," tutup mantan Dirut PLN ini.
(dru/dnl)

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Palm | Kelapa Sawit

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Industri Miyak Kelapa Sawit | Palm Oil Industri Overview

Palm Oil Milling Process

Edible Oil Processing - Production

PALM OIL MILLING PROCESS

Introduction

Sterilisation

Stripping

Digestion and Pressing

Clarification

Decanters

Oil Losses during Processing

Kernel Production

Biomass

Table 1. Dry basis calorific value of palm waste materials (Source: Yap, 2010).

Treatment of Raw Palm Oil Mill Effluent (POME)

References

Asian Agri Group | Alamat Asian Agri | Asian Agri Medan | Jakarta

Dalam Dua Bulan, Astra Jual 201.753 Ton Sawit

Penjualan Komoditas Perkebunan Naik, JAWA Cetak Laba Rp 185 miliar

Menteri BUMN Dahlan Iskan | Manfaatkan Perkebunan Sawit dalam Meningkatkan Produksi Sapi

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