Unit Cost Iplc

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U NI TC OSTI P LC U N I TC O S TIP LC D ISAMP AI K AN O LEH : EDYH AN D A D IS AMP AIK AN O LEH : ED YH AN D A  Y  Y  A NT O  ANTO BBTKLPPY O G Y AKAR T A BBTKLPPY O G Y AKAR T A D I S EL EN G G ARAK AN O LE H D I S ELE N G G AR AKAN O L EH BB K BBK K K P P  YOG Y AK AR T A  Y O G Y A K A RT A JU N I J U NI 2 01 201 4 4

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UNIT COST IPLCUNIT COST IPLC

DISAMPAIKAN OLEH : EDY HANDADISAMPAIKAN OLEH : EDY HANDA Y Y ANTO ANTO

BBTKLPP YOGYAKARTABBTKLPP YOGYAKARTA

DISELENGGARAKAN OLEHDISELENGGARAKAN OLEH

BBKBBKKKPP YOGYAKARTA YOGYAKARTA

JUNIJUNI20120144

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RASIO PELAYANAN PDAM(KIMPRASWIL TAHUN 2003)

1. Metropolitan 210 lt/Orang/hari.

2. Kota besar 170 lt/Orang/hari.

3. Kabupaten 150 lt/Orang/hari.

CATATAN : apat !iguna"an sebagai alternati# perhitungan !ebit $C

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%&'()T*N+AN &,)T $)M,A(

%a!a pela"sanaan sur-ei !ilapangan uuna untu"en!apat"an !ata !ebit libah air sulit !i!apat

"euali pa!a )%$C ang su!ah engguna"an alat

pengu"ur !ebit $C.

*ntu" eu!ah"an per"iraan berapa !ebit $C !i '

perhari

Carana :

4ulah ,e! raat inap 6 500 lt !g bor ratarata 70 8shg per"iraan ost operasional )%$C !apat !ihitung.

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KOMPONEN BIAYA PENGOLAHAN LC RS

SECARA KIMIA DAN BIOLOGI

1.BAHAN (Koagulan, Urea, Stater bakteri).

2.PERALATAN (Pemeliharaan/Perawatan).

3.ENERGI (Pompa blower, Pompa lumpur, Mixer).

4.TENAGA (Cleaning S, Sanitarian).

5.Pengelolaan Limbah B3.

6.Uji Lapangan dan Lab

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MENGHITUNG KEBUTUHAN

PENGOLAHAN LC RS

CONTOH BAHAN :

Netralisasi LC Laundry (misalkan Q =

10 m³/hr).

PAC 50 gr/m³ x 10 = 500 gr = 0,5 kg/hrKapor 20 gr/m³ x 10 = 200 gr = 0,2 kg/hr

Nutrisi bakteri aerob/anaerob (misalkan

total Q =100 m³/hr).Urea 1 gr/m³ x 100 = 100 gr = 0,1 kg/hr.

Stater EM 1 lt/bln (stok).

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LANJUTAN

Nutrisi bakteri aerob/anaerob

(misalkan total Q =100 m³/hr).

Urea 1 gr/m³ x 100 = 100 gr = 0,1 kg/hr.

Stater EM 1 lt/bln (stok).

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LANJUTAN

1. KEBUTUHAN BAHAN PERHARI

Harga PAC = 15.000/kg X 0,5 kg = 7.500.

Harga CaO = 2.000/kg X 0,2 kg = 400.

Harga Urea= 2.500/kg X 0,1 kg = 250.

Harga EM = 90.000/lt : 30 hr = 3.000.

Jumlah = 11.150.

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LANJUTAN

2. ALAT (Pemeliharaan/Perawatan).

Terdiri :

 Kerusakan pompa

 Kerusakan alat Lab.  Kerusakan APD

 dll.

Standar anggaran (biaya) perawatan dihitung

5 – 10 % pertahun dari harga jumlah peralatan

yang digunakan di IPLC.

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LANJUTAN

3.ENERGI LISTRIK (Pompa blower, Pompa

lumpur dan Mixer).

Pompa blower 5 PK/3,52 kw untuk aerasi dibakaerob (bak lumpur aktif).

Pompa lumpur 0,5 PK/0,35 kw untuk resicle

lumpur dari bak pengendap ke bak aerob.

Mixer 0,5 PK/0,35 kw untuk koagulasi laundry

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LANJUTAN

ENERGI LISTRIK PERHARI.

(Pompa blower, Pompa lumpur , Mixer).

Restibusi listrik P.Blow= 3,520 x 24 x 1200 =102.000Restibusi listrik P.Lum = 0,35 x 24 x 1200 = 10.200

Restibusi listrik Mixer = 0,35 x 2 x 1200 = 800

Jumlah =113.000

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LANJUTAN

4.TENAGA (Cleaning S, Sanitarian).

Honor tiap hari = 100.000

5.Pengelolaan Limbah B3.

MoU dg pihak ke dua untuk

pengelolaan lumpur di drying bed.

Biaya tiap hari = 12.000/kg

6.Uji Lapangan dan Laboratorium.

Biaya tiap hari = 20.000.

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PERENCANAAN KEBUTUHAN

PENGOLAHAN LC RS DISETIAP UNIT

PENGOLAHAN

NO UNIT IPLC KEBUTUHAN JUMLAH

TIAP BULAN1 Netralisasi

Laundry

PAC

Kapor

?

2 Bak Biologi Urea

EM/ stater bakt

?

3 Pengujian LC Uji Lap/Lab ?

4 Pengelolaan

lumpur B3

MoU pihak ke 2 ?

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MENGHITUNG TOTAL UNIT COST IPLC RS

(Q = 100 M³ PER HARI)

1. BAHAN = 11.150.

2. PERALATAN = ?

3. ENERGI LISTRIK = 113.000.

4. TENAGA = 100.000.5. PENGELOLAAN LB3 = 12.000.

6. Uji Lapangan dan Lab. = 20.000.

  JUMLAH = 245.000.

Jadi tiap 1 m³ LC untuk biaya pengolahannya =

 245.000. : 100 = 2.450.

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LANJUTAN

,iaa tsb belu terasu" :

1. %&N9**TAN %&'A$ATAN )%$C AN $A,.

2. %&N9**TAN ,AN+*NAN )%$C.

3. %&N9**TAN 4A')N+AN )T'),*)

%&'%)%AAN.

. &N&'+) $)T')K $A)NN9A.

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%&N9**TAN %&'A$ATAN )%$C 9AN+

,&$*M MA*K %&'()T*N+AN

O)N+ %*M% %OM%A ,$O;&'

M)6&'

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)%$A9 '&)* K$O')N < C$ 2 =

$an>utan

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MODEL ALAT PH, TDS, DO METER

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MODEL ALAT JAR TEST

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GLASS WARE DAN BOTOL SEMPROT

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 ALAT KERUCUT IMHOFF

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