2AZ-FE 2.4L
TID $07: A/F SENSOR HEATER
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| 1 | $01 | Multiply by 0.00017 (A) | Maximum heater current (Bank 1) | Malfunction criterion for A/F sensor heater |
TID $04: HO2S HEATER
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| 1 | $02 | Multiply by 0.000076 (A) | Maximum HO2S heater current (Bank 1 Sensor 2) | Malfunction threshold for HO2S heater |
TID $08: THERMOSTAT
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| 1 | $01 | Multiply by 0.625 and subtract 40 (°C) | ECT sensor output when estimated ECT has reached to malfunction criterion | Malfunction criteria for thermostat |
O2S TEST RESULT
| Test ID | Test Item | Description | Unit Conversion | Unit | Standard Value |
|---|---|---|---|---|---|
| $07 | MIN HO2S V | Minimum HO2S voltage | Multiply by 0.005 | V | Less than malfunction threshold |
| $08 | MAX HO2S V | Maximum HO2S voltage | Multiply by 0.005 | V | More than malfunction threshold |
| $31 | Time $31 | HO2S switch time from Lean to Rich | Multiply by 0.04096 | second | Less than malfunction threshold |
| $32 | Time $32 | HO2S switch time from Rich to Lean | Multiply by 0.04096 | second | Less than malfunction threshold |
| $37 | Time $37 | Time that HO2S voltage drops to 0.2 V after fuel-cut begins | Multiply by 0.04096 | second | Less than malfunction threshold |
| $81 | Time $81 | Percentage in monitor time when HO2S voltage is lower than 0.05 V | Multiply by 0.3906 | % | Less than malfunction threshold |
| $84 | Time $84 | Percentage in monitor time when HO2S voltage is 0.7 V or higher | Multiply by 0.3906 | % | More than malfunction threshold |
| $85 | Time $85 | Maximum time while HO2S voltage exceeded 0.45 V continuously | Multiply by 0.2621 | seconds | More than malfunction threshold |
| $87 | Time $87 | Percentage in monitor time when HO2S voltage is 0.45 V or higher | Multiply by 0.3906 | % | More than malfunction threshold |
TID $01: CATALYST - SENSOR 1 A/F SENSOR, SENSOR 2 HO2S
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| 0 | $01 | Multiply by 0.0078 (no dimension) | Catalyst deterioration level (bank 1): Determined by waveforms of A/F sensor and HO2S 2 |
Malfunction criteria for catalyst deterioration |
A/F SENSOR
| MID | TID | Scaling | Description of Test Value | Minimum Test Limit | Maximum Test Limit |
|---|---|---|---|---|---|
| $01 | $91 | Multiply by 0.003 [mA] | Air-fuel ratio sensor current or bank 1 sensor 1 | Malfunction criterion for low side rationality | Malfunction criterion for high side rationality |
TID $06: A/F SENSOR
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| 0 | $01 | Multiply by 0.000244 (no dimension) | Parameter for identify A/F sensor response rate (Bank 1) | Malfunction threshold for A/F sensor deterioration |
EVAP
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit | ||
|---|---|---|---|---|---|---|
| 1 | $01 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for small leak (P0456):) Refer to pressure D(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $02 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for gross leak (P0455): Refer to pressure E(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $03 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for vacuum pump stuck OFF (P2401): Refer to pressure A(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $04 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for vacuum pump stuck ON (P2402): Refer to pressure A(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $05 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for vent valve stuck OFF (vent) (P2420): Refer to pressure C(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $06 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for vent valve stuck ON (closed) (P2419): Refer to pressure A(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $07 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for 0.02 inch orifice low flow (P043E): Refer to pressure B(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $08 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for 0.02 inch orifice high flow (P043F): Refer to pressure A(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $11 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for purge VSV stuck close (P0441): Refer to pressure F(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $12 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for purge VSV stuck open (P0441): Refer to pressure E(1) |
Malfunction criteria (0 kPa) | ||
| 1 | $13 | Multiplied by 0.0156 subtract 2 (kPa) | Test value for purge flow (P0441): Refer to pressure G(1) |
Malfunction criteria (0 kPa) | ||
|
||||||