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 | Malfunction criterion for A/F sensor heater |
TID $07: A/F SENSOR HEATER TEST
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| 1 | $02 | Multiply by 0.00076 (A) | Maximum HO2S heater current (Bank 1 Sensor 2) | Malfunction criterion 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 substract 40 (°C) | ECT sensor output when estimated ECT has reached to malfunction criterion | Malfunction criteria for thermostat |
HO2S OUTPUT VOLTAGE (MINIMUM AND MAXIMUM)
| TEST ID | Description of TEST VALUE | Conversion Factor (Unit) | Unit | Standard Value |
|---|---|---|---|---|
| $07 | Minimum HO2S voltage | N/A | V | Less than TEST LIMIT |
| $08 | Maximum HO2S voltage | N/A | V | More than TEST LIMIT |
| $31 | Minimum time per one cycle of HO2S frequency that HO2S switches Lean to Rich | N/A | Second | Less than TEST LIMIT |
| $32 | Minimum time per one cycle of HO2S frequency that HO2S switches Rich to Lean | N/A | Second | Less than TEST LIMIT |
| $37 | Time until HO2S voltage drops to 0.2 V during fuel-cut | N/A | Second | Less than TEST LIMIT |
| $81 | Percentage in monitoring time while HO2S voltage is lower than 0.05 V | Multiply 0.39 | % | Less than TEST LIMIT |
| $84 | Percentage in monitoring time while HO2S voltage is higher than 0.7 V | Multiply 0.39 | % | More than TEST LIMIT |
| $85 | Continuous time while HO2S voltage is higher than 0.45 V | Multiply 0.262 | Second | More than TEST LIMIT |
| $87 | Percentage in monitoring time while HO2S voltage is higher than 0.45 V | Multiply 0.39 | % | More than TEST LIMIT |
TID $01: CATALYST - SENSOR 1 A/F SENSOR, SENSOR 2 HO2S
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| O | $01 | Multiply by 0.0078 (no dimension) | Catalyst deterioration level: Determined by waveforms of A/F sensor and HO2S | Malfunction criteria for catalyst deterioration |
TID $06: A/F SENSOR TEST
| TLT | CID | Unit Conversion | Description of Test Data | Description of Test Limit |
|---|---|---|---|---|
| O | $01 | Multiply by 0.000244 (no dimension) | Parameter for identify A/F sensor response rate | Malfunction threshold for A/F sensor deterioration. |
TID $02: EVAP SYSTEM (KEY-OFF MONITOR)
| 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) | ||
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